Journal Information
Vol. 8. Issue 6.
Pages 5140-5148 (November - December 2019)
Download PDF
More article options
Vol. 8. Issue 6.
Pages 5140-5148 (November - December 2019)
Original Article
DOI: 10.1016/j.jmrt.2019.08.037
Open Access
Investigation into the flotation of malachite, calcite and quartz with three phosphate surfactants
Hongli Fan, Jingqin Qin, Jun Liu, Guangyi Liu
Corresponding author

Corresponding author.
, Xianglin Yang
College of Chemistry and Chemical engineering, Central South University, Changsha, 410083, China
Article information
Full Text
Download PDF
Figures (15)
Show moreShow less
Tables (3)
Table 1. Relative atomic concentration of elements as confirmed by XPS.
Table 2. High-resolution of Cu 2p 3/2 XPS.
Table 3. High-resolution P 2p XPS.
Show moreShow less

The flotation response of malachite, calcite and quartz to bis (2-ethylhexyl) phosphate (DEHPA), dibutyl phosphate (DBP) and tributyl phosphate (TBP) was evaluated by micro-flotation experiments. The results showed that DEHPA exhibited an impressive flotation selectivity for malachite against calcite/quartz in the pH range of 6.0–9.0 and achieved superior malachite flotation recovery over DBP and TBP. The flotation mechanism of DEHPA to malachite was farther investigated through adsorption, contact angle, zeta potential, Fourier transform infrared spectroscopy (FTIR) and X-ray photoelectron spectroscopy (XPS). The findings inferred that DEHPA reacted with the surface copper atom of malachite via its O atoms of POH and PO to form the hydrophobic surface complexes of Cu(II)-DEHPA. The double active center of the P(O)OH group might be contributed to the stronger affinity of DEHPA and DBP to malachite than that of TBP with the single active center of the PO group. TBP returned the lowest malachite recovery among the three phosphate surfactants, even it has more hydrophobic-carbon atoms than those of DBP.

Bis (2-ethylhexyl) phosphate
Full Text

Copper is extensively used in daily necessities, industries and national defenses. Copper oxide minerals are of a significant resource for copper production [1,2]. Currently, there are two basic technologies for the processing of copper oxide minerals, leaching/solvent extraction/electrowinning process and froth flotation. The former usually is a time-consuming and costly process with high pollution and low processing capacity [3,4]. In many cases, flotation technology is a better choice for the separation and enrichment of copper oxide minerals [5–8].

Malachite [Cu2(OH)2CO3] is the most common CuO mineral in the copper oxide deposits. For possessing dissolubility and hydration, malachite exhibits a poor floatability during froth flotation process [9,10]. It is well established that in froth flotation, collectors play a bridge role between mineral particles and bubbles [11,12]. Thus, to develop high-performance collectors for malachite flotation is of great importance for improving its separation and enrichment.

For flotation recovery of malachite, there are two general technologies, pre-sulfidization flotation with sulfydryl collectors such as xanthates [13–18] and direct flotation with oxide mineral collectors including fatty acids, fatty amines, petroleum sulfonates and hydroxamic acids [18–22]. In most cases, the former is more effective than the latter. However, the pre-sulfidization flotation suffers from the insufficient or excessive sulfidization, leading to the unsatisfied flotation separation efficiency of malachite [13,14,19,20]. Therefore, to separate and enrich malachite through direct flotation approaches has been widely investigated, and the high-selective collectors toward malachite have been far from being satisfactory [23,24]. A great number of investigations showed that the phosphoric acid compounds exhibited strong affinity toward metal oxides through the formation of MOP bonds [25–27], and their surfactants have been widely used in the flotation of metal oxide minerals. Bulatovic et al. thought the dialkyl phosphoric acid esters were effective collectors for the flotation recoveries of titanium minerals [28,29]. And they found that octyl diphosphonic acid possessed pretty good selectivity for niobite flotation [29]. Kirchberg and Wottgen observed that alkyl phosphoric acids with 5-7 carbon atoms in their alkyl group were powerful flotation collectors for fine cassiterite [30]. Despite the widespread application of phosphorous surfactants in froth flotation of metal oxide minerals, little is known about their flotation separation of malachite from calcite or quartz.

In this paper, bis (2-ethylhexyl) phosphate (DEHPA) was introduced as a flotation collector to enrich malachite, calcite or quartz. Its flotation performances were compared with those of dibutyl phosphate (DBP) and tributyl phosphate (TBP) by micro-flotation tests. Subsequently, the adsorption mechanism of DEHPA toward malachite surfaces was investigated through adsorption, contact angle, zeta potential, Fourier transform infrared spectroscopy (FTIR) and X-ray photoelectron spectroscopy (XPS)

2Materials and methods2.1Materials

DEPHA and TBP were purchased from Aladdin and DBP was obtained from Xiya Reagents. Their molecule structures were shown in Fig. 1. Other reagents used in the experiments were purchased from commercial suppliers and they were all analytical reagent grade. Distilled water was used in all the experimental processes.

Fig. 1.

Molecule structures of DEPHA (a), DBP (b) and TBP (c).


Malachite, calcite and quartz with high purity were obtained from Guilin, Guangxi Province, China [31]. After being ground and sieved, the mineral particles with a diameter ranging from +37 to −74 μm were used in the micro-flotation and adsorption tests. The finer part of −5 μm was used for the measurements of zeta potential, FTIR and XPS.

2.2Micro-flotation tests

A 240 mL Hallimond tube was used to perform the micro-flotation tests. The flotation procedure was according to our previous experiment [24]. After conducting flotation for 3 min under 200 ± 2 mL/min N2, the froth and underflow products were separately collected, filtered, dried and then weighed. The flotation recovery was calculated by Eq. (1).

Here, ε is the recovery of malachite, calcite or quartz, m1 and m2 are the weight of the froth and underflow products (g), respectively. The listed recovery was the average of two independent tests.

2.3Zeta potential measurements

Zeta potential of malachite, calcite or quartz particles with or without DEHPA in 1 × 10−2 mol/L KCl solution was recorded at 298 ± 1.5 K on the Brookhaven Zeta Plus analyzer (USA) [24]. 50 mg mineral samples and DEHPA solutions were mixed. To obtain the desired pH of the suspension, several drops of dilute KOH or HCl solutions were injected. Afterwards, the suspension was agitated for 5 min and its zeta potential was independently measured eight times. Their average value was reported with a common variation of ±5 mV.

2.4Adsorption and contact angle measurements

To a 150 mL conical flask, 0.1 g malachite, 20 mL distilled water, desired pH regulators (dilute KOH or HCl solutions), DEPHA solutions, and extra distilled water were sequentially added to reach 100 mL. After shaking the suspension for 4 h at 298 ± 1.5 K, the malachite pulp was filtered, and the residual concentration of DEPHA in the filtrate was measured according to the concentration of total organic carbon recorded by the Total Organic Carbon analyzer (TOC-VCPH, Shimadzu, Japan). The adsorption amount of DEPHA on malachite surfaces was calculated via Eq. (2)

Here, Qe is the amount of DEPHA covered on malachite (mol/m2), Co is DEPHA’s initial concentration (mol/L), Ce is the residual concentration of DEPHA (mol/L), V is the volume (L), S is malachite’s specific surface area with a value of 0.346 m2/g, and W is the mass of malachite (g). Each adsorption test was repeated twice, independently, and the average result was reported.

The contact angles of malachite surfaces with/without DEPHA modification were measured via water drop method on the Zhongchen JC2000C device (China) [12]. The average value of five separate measurements was reported.

2.5FTIR and XPS measurements

2 × 10−4 mol/L DEHPA solutions were blended with 2 × 10−4 mol/L CuSO4 solutions in a volume proportion of 1:2. After being stirred, a blue precipitate appeared from the mixture. 50 mg malachite particles were stirred in 100 mL 2 × 10−4 mol/L DEHPA solutions for 5 h at 298 ± 1.5 K. Afterwards, the malachite particles and the blue precipitates were separately filtered, rinsed a couple of times with water, desiccated in a vacuum chamber for 5 days, and then delivered for FTIR and XPS detections.

The Nicolet FTIR-740 spectrometer (USA) was adopted for FTIR record by KBr disk method. And the wavenumber was ranged from 500 to 4000 cm−1 with a resolution of 4 cm−1.

The ESCALAB 250 Xi instrument and Avantage soft of Thermo Scientific (USA) were used to record and analyze the XPS spectra [24]. And the XPS binding energy was calibrated by setting the C 1s XPS peak at 284.6 eV.

3Results and discussion3.1Micro-flotation findings

Fig. 2 shows the flotation response of malachite, calcite and quartz to pH with 1 × 10−5 mol/L DEHPA, DBP or TBP. The results of Fig. 2 (a) indicate that in the presence of 1 × 10−5 mol/L DEHPA, the flotation recovery of malachite was over 90% in the pH range of 6–11, while quartz recovery was less than 25%. As for the calcite, a relatively low flotation recovery was observed at pH 6–9. When the pH values were higher than 9, calcite recovery increased sharply and reached the maximum of ∼82% at pH around 10. The flotation results indicated that DEHPA exhibited excellent flotation selectivity toward malachite against calcite and quartz at pH 6–9.

Fig. 2.

Flotation response of malachite, calcite and quartz to pH with 1 × 10−5 mol/L DEHPA (a), DBP (b) and TBP (c).


Fig. 2 (b) demonstrates that 1 × 10−5 mol/L DBP recovered approximate 65% malachite over the pH range of 7–9. And malachite recovery decreased to below 60% at pH ∼ 6 or over 10. However, the lower flotation recovery for calcite or quartz was observed across the experimental pH range of 6–11. Obviously, the flotation performance of DBP for malachite was inferior to that of DEHPA.

In Fig. 2 (c), 1 × 10−5 mol/L TBP recovered less than 45% malachite, 35% calcite or 25% quartz at pH 6–11. This meant that TBP owned weak collecting power toward malachite, calcite and quartz.

The flotation response of malachite, calcite or quartz as a function of the initial concentration of DEHPA, DBP or TBP at pH ∼7 was listed in Fig. 3. It shows that the recoveries of the three minerals increased as increasing collector concentration from 1 × 10−6 to 1 × 10−5 mol/L. At 1 × 10−5 mol/L collector, the recovery of malachite was near 95%, 63% and 43% for DEHPA, DBP and TBP, respectively, while, the flotation recoveries of calcite or quartz were below 30%.

Fig. 3.

Flotation recoveries of malachite, calcite and quartz as a function of DEHPA (a), DBP (b) and TBP (c) initial concentration (at pH ∼7).


Therefore, Figs. 2 and 3 indicate that the flotation performances of the three phosphate collectors toward malachite could be determined as: DEHPA > DBP > TBP. Specifically, DEHPA exhibited excellent flotation selectivity for malachite versus calcite and quartz over the pH range of 6–9.

For DEHPA and DBP, they possess the active center of P(O)OH, and DEHPA returned the higher malachite flotation recoveries for its longer carbon chain and stronger hydrophobicity. TBP owns the PO functional group which might exhibit weak affinity to copper atom in comparison to the P(O)OH group, returning the lowest malachite recoveries among the three phosphate surfactants, even it has more hydrophobic-carbon atoms than those of DBP [32].

3.2Zeta potential results

Fig. 4 shows the isoelectric point (IEP) of the malachite fine particles occurred at pH ∼ 8.4, near the reported values [12,33]. In the presence of 1 × 10−4 mol/L DEHPA, malachite’s ζ (zeta potential) significantly moved to more negative values, and its IEP emerged at pH ∼6.7, which implied the adsorption of DEHPA onto the copper atom sites (positive charges sites) of malachite interfaces.

Fig. 4.

The zeta potential of malachite fine particles with and without 1 × 10−4 mol/L DEHPA.


The pKa (the negative logarithm of acid dissociation constant) value of DEHPA was about 1.72 [12,33,34], indicating that the dominated species of DEHPA in aqueous solutions at pH > 6 is its anion ((C8H17O)2POO). Thus, at pH 6.0–8.4, electrostatic attraction might drive the adsorption of DEHPA onto malachite surfaces. Given that malachite particles were negatively charged at pH > 8.4, the electrostatic attraction was unlikely to be the main driving force for malachite adsorption of anionic DEHPA. However, it was experimentally observed from Fig. 4 that the anionic DEHPA did adsorb onto malachite surfaces at pH > 8.4. These phenomena clearly inferred that DEHPA adsorption overcame the electrostatic repulsive force, recommending a coordination bonding effect of anionic DEHPA to the interface Cu atom on malachite.

3.3Adsorption results

The adsorption quantities of DEHPA on malachite as a function of pH or DEHPA dose are shown in Fig. 5. Fig. 5 (a) presents that under 1 × 10−5 mol/L DEHPA, the preferable pH for malachite adsorption of DEHPA occurred around 7.0. Fig. 5 (b) demonstrates that at pH ∼7.0, malachite adsorption towards DEHPA swiftly increased with the increasing concentration until reaching 1 × 10−5 mol/L DEHPA. Sequentially, the increase of DEHPA’s adsorption amount turned very slow.

Fig. 5.

Adsorption amount of DEHPA on malachite surfaces as a function of pH (a) (CDEHPA = 1 × 10−5 mol/L) or initial dose (b) (at pH ∼7).

3.4Contact angle

Contact angle is an important index for characterizing the hydrophobicity of a mineral surface. The hydrophobization ability of a collector toward a given mineral surface is closely related to its flotation performance [12,33].

The newly-polished malachite exhibited the contact angle of 42 ± 1°. After 1 × 10−5 mol/L DEHPA modification of 10 min, malachite’s contact angle increased as shown in Fig. 6. Fig. 6 also demonstrates that the maximum water contact angle of malachite emerged at pH around 7.0 with a value of 93.5 ± 0.5°, which corresponded to the preferable pH for malachite adsorption of DEHPA.

Fig. 6.

Contact angle of malachite as a function of pH (under 1 × 10−5 mol/L DEHPA).


The FTIR spectra for DEHPA, Cu-DEHPA sediments, and malachite without/with DEHPA treatment are respectively shown in Fig. 7.

Fig. 7.

FTIR spectra of (a) DEHPA before or after its response to Cu2+ and (b) malachite before and after DEHPA adsorption.


Fig. 7 (a) indicates that for DEHPA, its CH vibrations of the CH2− and CH3− groups arose on about 2865, 2930 and 2961 cm−1. The peaks near 1031 and 886 cm−1 were respectively attributed to its POC and POC vibrations [35]. The characteristic band being close to 2326 cm−1 was related to its POH oscillation [36]. And its PO and POH adsorption bands separately appeared close to 1226 and 1690 cm−1[37–41]. For Cu-DEHPA sediments, the adsorption peaks near 2864, 2930 and 2960 cm−1 were due to the CH vibrations. The

vibration bands appeared close to 1182 cm−1[37]. The peaks at ∼1029 and 1098 cm−1 belonged to POC vibrations and those at 884 cm−1 due to POC oscillations. The characteristic bands near 3448 and 1633 cm−1 resulted from the OH vibrations of water molecules [4,40].

After modification with DEHPA, the CH adsorption bands at around 2850, 2920 and 2960 cm−1 appeared on malachite as presented in Fig. 7(b) [41]. The vibration peak at ∼1628 cm−1 might be related to OH of water molecules. It should be noted that malachite possesses strong IR adsorption bands which covered those of Cu-DEHPA surface complexes, thus making their characteristic absorption peaks less pronounced [41].

3.6XPS results

The XPS for the Cu-DEHPA precipitation and malachite modified by DEHPA are shown in Figs. 8–10 and Tables 1–3. The survey XPS results in Fig. 8 and Table 1 demonstrate that the mole ratio of carbon, oxygen, phosphorus and copper in the Cu-DEHPA precipitates was of 31.95:9.00:2.10:1.00, suggesting that the chemical composition of the Cu-DEHPA precipitates was of Cu(DEHPA)2·H2O. This meant two DEHPA species might combine with one copper atom to form Cu-DEHPA complexes [42]. After malachite was treated with DEHPA, its atomic concentration of carbon and phosphorus increased, while that of copper and oxygen reduced, signifying the adsorption of malachite towards DEHPA.

Fig. 8.

The scanning XPS of malachite before (a) and after (b) DEHPA adsorption, and Cu-DEHPA precipitate (c).

Table 1.

Relative atomic concentration of elements as confirmed by XPS.

SubstancesRelative atomic concentration/%
C 1 s  O 1 s  Cu 2p  P 2p 
Cu-DEHPA precipitate  72.53  20.44  2.27  4.76 
Malachite  28.96  48.97  21.72  0.34 
Malachite after DEHPA adsorption  35.05  46.88  16.46  1.61 
Δa  6.09  −2.09  −5.26  1.27 

Δ is defined as the difference value of atomic concentration.

As shown in Fig. 9 and Table 2, the Cu 2p3/2 XPS peaks of the Cu-DEHPA precipitation were observed at ∼934.71 and 932.43 eV, which might be separately assigned to the Cu(II)-DEHPA1 with the

structure and the Cu (II)-DEHPA2 with the
configuration. The Cu 2p3/2 XPS peaks for malachite appeared around 934.65 eV, belonging to Cu(II) oxides [43]. After treatment with DEHPA, malachite surface existed two XPS adsorption bands at ∼934.72 and 932.65 eV, the former might be designated as the Cu(II)-DEHPA1 with the
configuration and the Cu(II) species in malachite bulk phase. The other might be assigned to the Cu(II)-DEHPA2 with the
configuration. The Cu atom in Cu(II)-DEHPA2 is more convenient to share electrons from its four-membered ring structure than that in Cu(II)-DEHPA1, resulting in lower Cu binding energy. It should be noted that during the interaction of DEHPA with malachite, its surface copper atoms acted as the reactive entities with the partly-exposed dangling bonds, which were significantly different from the free cupric ions in aqueous solutions during the generation of Cu-DEHPA precipitation, probably resulting in the higher proportion of Cu(II)-DEHPA2 in the precipitates than that in the DEHPA complexes on malachite surfaces.

Fig. 9.

High-resolution Cu 2p 3/2 XPS for malachite (a) before and (b) after DEHPA treatment, and (c) Cu-DEHPA precipitate.

Table 2.

High-resolution of Cu 2p 3/2 XPS.

Substance  Binding energy/eV  Half peak width/eV  Atomic concentration/%  Affiliation 
Malachite  934.65  2.80  100  Cu(II) 
Malachite covered by DEHPA  934.72932.65  2.73 1.77  64.52 35.48  Cu(II), Cu(II)-DEHPA1Cu(II)-DEHPA2 
Cu-DEHPAprecipitate  934.71932.43  2.56 1.51  32.89 67.11  Cu(II)-DEHPA1Cu(II)-DEHPA2 

The P atom of DEHPA has a valence of 5 [44–46]. Fig. 10 and Table 3 show that the P 2p XPS bands for the Cu-DEHPA precipitation and the DEHPA-treated malachite were divided into two peaks at ∼134.15 eV and 133.36 eV, respectively. The lower-energy peak might be belonged to P(V) in the Cu(II)-DEHPA2 configuration and the higher was owing to P(V) in the Cu(II)-DEHPA1. The P 2p and Cu 2p3/2 XPS adsorption bands implied that there might be two bonding models of DEHPA with copper atom in the Cu-DEHPA precipitation and Cu-DEHPA surface complexes. Surely, to confirm the exact bonding structure between DEHPA and copper needs further investigations.

Fig. 10.

High-resolution P 2p XPS bands for (a) malachite after DEHPA treatment and (b) Cu-DEHPA precipitate.

Table 3.

High-resolution P 2p XPS.

Substance  Binding energy/eV  Half peak width/eV  Atomic concentration/%  Affiliation 
DEHPA-treated Malachite  134.13133.32  1.77 1.33  64.52 35.48  P(V) species in Cu(II)-DEHPA1P(V) species in Cu(II)-DEHPA2 
Cu-DEHPA precipitate  134.15133.36  1.24 1.21  37.11 62.89  P(V) species in Cu(II)-DEHPA1P(V) species in Cu(II)-DEHPA2 

The flotation performances of DEHPA to malachite, calcite and quartz were compared with those of DBP and TBP by micro-flotation tests, and DEHPA’s adsorption mechanism towards malachite was further explored via adsorption, contact angle, zeta potential, FTIR and XPS. Based on the experimental findings, the following conclusions were recommended:

The micro-flotation results demonstrated the collecting affinity of the three phosphate collectors toward malachite could be determined as: DEHPA > DBP > TBP. And, DEHPA exhibited excellent flotation selectivity for malachite versus calcite and quartz over the pH range of 6–9.

Contact angle results illustrated that the hydrophobicity of malachite surface was significantly improved after DEHPA treatment. Adsorption experiments indicated that the preferable pH for malachite adsorption of DEHPA emerged at pH around 7.0, corresponding to that of contact angle findings. Zeta potential inferred that DEHPA might adsorb onto malachite surfaces via electrostatic interaction under pH 6–8.4. At pH > 8.4, the coordination bonding effect might be the dominated driving force for malachite adsorption of DEHPA.

FTIR and XPS inferred that DEHPA reacted with the surface copper atom of malachite via its O atoms of POH and PO. The double active center of the P(O)OH group might be contributed to the stronger affinity of DEHPA to malachite than that of TBP with the single active center of the PO group. The Cu(II)-DEHPA chemisorption layers on malachite surfaces improved the hydrophobicity of malachite particles and realized their flotation enrichment.


The authors would like to thank the National Natural Science Foundation of China [51474253] and the National Basic Research Program of China (973 program) [2014CB643403] for the financial support.

J. Deng, S. Wen, Q. Yin, D. Wu, Q. Sun.
Leaching of malachite using 5-sulfosalicylic acid.
J Taiwan Inst Chem E, 71 (2017), pp. 20-27
T. Deng, J. Chen.
Treatment of oxidized copper ores with emphasis on refractory ores.
Min Proc Ext Met Rev, 7 (1991), pp. 175-207
K. Lee, D. Archibald, J. McLean, A.M. Reuter.
Flotation of mixed copper oxide and sulphide minerals with xanthate and hydroxamate collectors.
Miner Eng, 22 (2009), pp. 395-401
J.S. Lee, D.R. Nagaraj, J.E. Coe.
Practical aspects of oxide copper recovery with alkyl hydroxamates.
Miner Eng, 11 (1998), pp. 929-939
N. Ahmed, G.J. Jameson.
Flotation kinetics.
Miner Process Extr M, 5 (1989), pp. 77-99
A.A. Abramov, K.S.E. Forssberg.
Chemistry and optimal conditions for copper minerals flotation: theory and practice.
Min Proc Ext Met Rev, 26 (2005), pp. 77-143
M. Gharai, R. Venugopal.
Modeling of flotation process—an overview of different approaches.
MIN PROC EXT MET REV., 37 (2016), pp. 120-133
X. Chen, Y. Peng.
Managing clay minerals in froth flotation—a critical review.
Min Proc Ext Met Rev, 39 (2018), pp. 289-307
X. Sun, B. Chen, Y. Yang, Y. Liu.
Technological conditions and kinetics of leaching copper from complex copper oxide ore.
J Cent South Univ T, 16 (2009), pp. 936
Q. Feng, W. Zhao, S. Wen, Q. Cao.
Copper sulfide species formed on malachite surfaces in relation to flotation.
J Ind Eng Chem, 48 (2017), pp. 125-132
P.I. Ecrola, V. Paloaari.
Developments in selective flotation of complex copper-lead-Zinc.
Min Proc Ext Met Rev, 15 (1995), pp. 47
G. Liu, Y. Huang, X. Qu, J. Xiao, X. Yang, Z. Xu.
Understanding the hydrophobic mechanism of 3-hexyl-4-amino-1, 2, 4-triazole-5-thione to malachite by ToF-SIMS, XPS, FTIR, contact angle, zeta potential and micro-flotation.
Colloids Surf A Physicochem Eng Asp, 503 (2016), pp. 34-42
S. Castro, J. Goldfarb, J. Laskowski.
Sulphidizing reactions in the flotation of oxidized copper minerals, I. Chemical factors in the sulphidization of copper oxide.
Int J Miner Process, 1 (1974), pp. 141-149
R. Zhou, S. Chander.
Kinetics of sulfidization of malachite in hydrosulfide and tetrasulfide solutions.
Int J Miner Process, 37 (1993), pp. 257-272
J. Xiao, N. Di, G. Liu, H. Zhong.
The interaction of N-butoxypropyl-N′-ethoxycarbonylthiourea with sulfide minerals: scanning electrochemical microscopy, diffuse reflectance infrared Fourier transform spectroscopy, and thermodynamics.
Colloids Surf A Physicochem Eng Asp, 456 (2014), pp. 203-210
L. Deng, S. Wang, H. Zhong, G. Liu.
N-(6-(hydroxyamino)-6-oxohexyl) decanamide collector: flotation performance and adsorption mechanism to diaspore.
Appl Surf Sci, 347 (2015), pp. 79-87
C. Marion, A. Jordens, R. Li, M. Rudolph, K.E. Waters.
An evaluation of hydroxamate collectors for malachite flotation.
Sep Purif Technol, 183 (2017), pp. 258-269
J. Xiao, G. Liu, H. Zhong.
International Journal of Mineral Processing the adsorption mechanism of N-butoxypropyl-S-[2-(hydroxyimino) propyl] dithiocarbamate ester to copper minerals flotation.
Int J Miner Process, 166 (2017), pp. 53-61
S.M. Bulatovic.
19–Flotation of oxide copper and copper cobalt ores.
pp. 47-65
G.A. Hope, A.N. Buckley, G.K. Parker, A. Numprasanthai, R. Woods, J. Mclean.
The interaction of n -octanohydroxamate with chrysocolla and oxide copper surfaces.
Miner Eng, 36 (2012), pp. 2-11
G.A. Hope, A. Numprasanthai, A.N. Buckley, G.K. Parker, G. Sheldon.
Bench-scale flotation of chrysocolla with n-octanohydroxamate.
Miner Eng, 36 (2012), pp. 12-20
H. Xu, H. Zhong, S. Wang, Y. Niu, G. Liu.
Synthesis of 2-ethyl-2-hexenal oxime and its flotation performance for copper ore.
Miner Eng, 66 (2014), pp. 173-180
S. Liu, G. Liu, H. Zhong, X. Yang.
The role of HABTC’s hydroxamate and dithiocarbamate groups in chalcopyrite flotation.
J Ind Eng Chem, 52 (2017), pp. 359-368
S. Liu, H. Zhong, G. Liu, Z. Xu.
Cu (I)/Cu (II) mixed-valence surface complexes of S-[(2-hydroxyamino)-2-oxoethyl]-N, N-dibutyldithiocarbamate: hydrophobic mechanism to malachite flotation.
J Colloid Interf Sci, 512 (2018), pp. 701-712
S. Marcinko, A.Y. Fadeev.
Hydrolytic stability of organic monolayers supported on TiO2 and ZrO2.
Langmuir, 20 (2004), pp. 2270-2273
G. Fonder, I. Minet, C. Volcke, S. Devillers, J. Delhalle, Z. Mekhalif.
Anchoring of alkylphosphonic derivatives molecules on copper oxide surfaces.
Appl Surf Sci, 257 (2011), pp. 6300-6307
C. Queffélec, M. Petit, P. Janvier, D.A. Knight, B. Bujoli.
Surface modification using phosphonic acids and esters.
Chem Rev, 112 (2012), pp. 3777-3807
S. Bulatovic, D.M. Wyslouzil.
Process development for treatment of complex perovskite, ilmenite and rutile ores.
Miner Eng, 12 (1999), pp. 1407-1417
G.L. Chen, D. Tao, H. Ren, F.F. Ji, J.K. Qiao.
An investigation of niobite flotation with octyl diphosphonic acid as collector.
Int J Miner Process, 76 (2005), pp. 111-122
S.I. Angadi, T. Sreenivas, H.S. Jeon, S.H. Baek, B.K. Mishra.
A review of cassiterite beneficiation fundamentals and plant practices.
Miner Eng, 70 (2015), pp. 178-200
J. Liu, Z. Hu, G. Liu, Y. Huang, Z. Zhang.
Selective flotation of copper oxide minerals with a novel amino-triazole-Thione surfactant: a comparison to hydroxamic acid collector.
Min Proc Ext Met Rev, (2019), pp. 1-11
A. Ghosh, D. Datta, H. Uslu, et al.
Separation of copper ion (Cu2+) from aqueous solution using tri n butyl phosphate and di (2-ethylhexyl) phosphoric acid as extractants.
J Mol Liq, 258 (2018), pp. 147-154
G. Liu, J. Xiao, J. Liu, X. Qu, Q. Liu, H. Zeng, et al.
In situ probing the self-assembly of 3-hexyl-4-amino-1, 2, 4-triazole-5-thione on chalcopyrite surfaces.
Colloids Surf A Physicochem Eng Asp, 511 (2016), pp. 285-293
S. Acharya, A. Nayak.
Separation of D2EHPA and M2EHPA.
Hydrometallurgy, 19 (1988), pp. 309-320
I.F. Amaral, P.L. Granja, M.A. Barbosa.
Chemical modification of chitosan by phosphorylation: an XPS, FT-IR and SEM study.
J Biomat Sci-Polym E, 16 (2005), pp. 1575-1593
A. Elias, M.A. Didi, D. Villemin.
Synthesis of mono-and dialkylphosphates by the reactions of hydroxycompounds with the phosphorus pentaoxide under microwave irradiation.
Phosphorus Sulfur Silicon Relat Elem, 179 (2004), pp. 2599-2607
B. Andrews, S. Almahdali, K. James, S. Ly, K.N. Crowder.
Copper oxide surfaces modified by alkylphosphonic acids with terminal pyridyl-based ligands as a platform for supported catalysis.
Polyhedron, 114 (2016), pp. 360-369
M. Nogami, M. Suwa, T. Kasuga.
Proton conductivity in sol-gel-derived P2O5-TiO2-SiO2 glasses.
Solid State Ion, 166 (2004), pp. 39-43
G. Socrates.
Infrared characteristic group frequencies.
Wiley-Interscience, (2000), pp. 241-246
W. Tan, G. Liu, J. Qin, H. Fan.
Hemimorphite flotation with 1-hydroxydodecylidene-1, 1-diphosphonic acid and its Mechanism.
Minerals, 8 (2018), pp. 38
J. Qin, G. Liu, H. Fan, W. Tan.
The hydrophobic mechanism of di(2-ethylhexyl) phosphoric acid to hemimorphite flotation.
Colloids Surf A Physicochem Eng Asp, 545 (2018), pp. 68-77
R. Grimm, Z. Kolařík.
Acidic organophosphorus extractants-XXV: properties of complexes formed by Cu(II), Co(II), Ni(II), Zn(II) and Cd(II) with di(2-ethylhexyl) phosphoric acid in organic solvents.
J Inorg Nucl Chem, 38 (1976), pp. 1493-1500
B.R. Strohmeier, D.E. Levden, R.S. Field, D.M. Hercules.
Surface spectroscopic characterization of Cu/Al2O3 catalysts.
J Catal, 94 (1985), pp. 514-530
F. Li, H. Zhong, H. Xu, H. Jia, G. Liu.
Flotation behavior and adsorption mechanism of α-hydroxyoctyl phosphinic acid to malachite.
Miner Eng, 71 (2015), pp. 188-193
P.H. Lo, W.T. Tsai, J.T. Lee, M.P. Hung.
Role of phosphorus in the electrochemical behavior of electroless Ni-P alloys in 3.5 wt.% NaCl solutions.
Surf Coat Tech, 67 (1994), pp. 27-34
T. Hanawa, M. Ota.
Calcium phosphate naturally formed on titanium in electrolyte solution.
Biomaterials, 12 (1991), pp. 67-74
Copyright © 2019. The Authors
Journal of Materials Research and Technology

Subscribe to our newsletter

Article options
Cookies policy
To improve our services and products, we use cookies (own or third parties authorized) to show advertising related to client preferences through the analyses of navigation customer behavior. Continuing navigation will be considered as acceptance of this use. You can change the settings or obtain more information by clicking here.