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Article

Rare Earth Metal Ion-Associates in Ln3+—CO32−—H2O System

1
The Department of General and Physical Chemistry, Empress Catherine II Saint Petersburg Mining University, 199106 Saint Petersburg, Russia
2
The Metallurgy Department, Empress Catherine II Saint Petersburg Mining University, 199106 Saint Petersburg, Russia
3
The Department of Chemical Engineering and Energy Processing, Empress Catherine II Saint Petersburg Mining University, 199106 Saint Petersburg, Russia
*
Author to whom correspondence should be addressed.
Metals 2025, 15(3), 239; https://doi.org/10.3390/met15030239
Submission received: 23 January 2025 / Revised: 19 February 2025 / Accepted: 22 February 2025 / Published: 24 February 2025

Abstract

This study focused on the nature of rare earth metal complex compounds that can form during the carbonate–alkaline processing of industrial waste materials, such as phosphogypsum and red mud, at 70–100 °C and 1–10 atm. Experimental findings revealed that the dissolution of synthetic carbonates of rare earth elements (REEs) in a concentrated carbonate-ion medium (3 mol/L) leads to the formation of ion-associates of varying strengths. Light (lanthanum, praseodymium, and neodymium) and medium (samarium) REE groups exhibited a tendency to form loose ion-associates, whereas heavy REEs (terbium, dysprosium, holmium, erbium, thulium, lutetium, and yttrium) formed close ion-associates. To confirm the existence of these ion-associates, the specific conductivity of solutions was measured after dissolving thulium (III) and samarium (III) carbonates at phase ratios ranging from 1:2000 g/mL to 1:40 g/mL in a potassium carbonate medium. The decay of ion-associates, leading to the precipitation of rare earth metal (III) carbonates, was tested in an ammonium carbonate medium. Thermal decomposition of ammonium carbonate at 70–75 °C during 1–4 h was accompanied by full rare earth carbonates’ sedimentation and its in-the-way separation into groups because of the varied strength of ion-associates. The results of this study provide a basis for developing processes to separate rare earth metals into groups during their carbonate–alkaline extraction into solution.

1. Introduction

Rare earth metals (REMs) are among the key types of strategic mineral resources, comprising 17 elements: 15 lanthanides, yttrium, and scandium [1,2,3]. The unique physicochemical properties of REMs enable their use in the production of permanent magnets, batteries, lasers, construction materials, alloys, catalysts, optical glasses, and various other products and intermediates. These materials are particularly essential in military industries, mechanical engineering, and medicine [4,5,6].
Among the existing classifications of REMs, the following are the most widely applied: [7,8]:
1.
By Mass
  • Light (La–Nd);
  • Medium (Sm–Gd);
  • Heavy (Dy–Lu, Y).
2.
By Importance, to eliminate the disbalance between global production and consumption of individual REEs
  • Critical (Nd, Eu, Tb, Dy, Er, Y);
  • Non-critical (La, Pr, Sm, Gd, Lu);
  • Surplus (Ce, Ho, Tm, Yb).
Monazite, xenotime, bastnasite, loparite, and other minerals serve as natural sources of surplus, non-critical, and critical REMs alike [9,10,11]. However, the generation of significant amounts of REM-containing industrial waste, such as phosphogypsum (PG) and red mud (RM), has made the recycling of secondary raw materials increasingly important [12,13,14]. Globally, PG reserves are estimated at 7–8 billion tons, while RM exceeds 4 billion tons, with REM content in these materials up to 0.9% [15,16,17].
Although the extraction of REMs and their compounds from traditional sources is predominantly achieved through acid-based methods, the processes developed over the past decades for processing PG and RM using mineral acids lack sufficient economic and/or environmental efficiency [18,19,20]. In this regard, the alternative carbonate–alkaline method—treatment with ammonium carbonate or alkali metal carbonate solutions—best meets modern requirements. However, it still requires optimization in terms of REMs’ extraction into solution and their subsequent separation [21,22].
The development of technical solutions for REM recovery remains constrained by the lack of definitive data on the forms of lanthanides, scandium, and yttrium in a carbonate-ion medium. Exceptions include a limited number of studies, such as those by Millero [23], Byrne [24], and others.
It is known that REMs in PG and RM can exist in the form of various sparingly soluble compounds: fluorides, sulfates, and phosphates in PG, and hydroxides and carbonates in RM [25,26]. REM cations (Ln3⁺), as well as the corresponding precipitates, are capable of forming carbonate complexes of variable composition, Ln(CO3)n3−2n, under the influence of an excess of carbonate ions. However, the structures of the resulting compounds remains uncertain [27,28,29].
On the one hand, the interaction of Ln3⁺ with CO32− (1) may involve the formation of classical coordination compounds, consisting of a central Ln ion and CO32− ligands. Under standard conditions, for n = 1, the stability constant K1 ranges from 6.52 to 9.15, and for n = 2 K2 it ranges from 11.58 to 17.41 [30,31,32]. Stability constants are presented in Table 1. On the other hand, the presence of a stability constant alone does not provide definitive evidence of a coordination compound.
Moreover, the nature of the bond between a REM ion and a carbonate anion remains unclear. Some researchers [33,34] suggest the possible formation of a complex in the form of an ion-associate (Figure 1), as follows:
L n ( a q ) 3 + + n C O 3 ( a q ) 2 L n ( C O 3 ) n ( a q ) 3 2 n
These forms are composed of particles held together by electrostatic attraction forces and comply with Coulomb’s law. Such behavior of lanthanides has been confirmed, for instance, for Yb3⁺ and Lu3⁺ ions in a Cl⁻ medium at concentrations exceeding 2 mol/L [34,35,36].
Thermodynamic evidence for the formation of ion pairs, triplets, and other structures lies in the high positive entropy values associated with the formation of ion-associates [33]. Due to the limited availability of literature data on the thermodynamics of the association processes involving REM cations and carbonate anions, the most analogous association process is (2), where the entropy of associate formation under standard conditions is 83 ± 12 J/(mol·K) [37]:
C a C O 3 ( s ) + C O 3 ( a q ) 2 C a ( C O 3 ) 2 ( a q ) 2
The entropy of formation for REM carbonate complexes under standard conditions, calculated using the Latimer–Powell equation, ranges from 159.9 J/(mol·K) to 266.9 J/(mol·K), which theoretically confirms the formation of Ln(CO3)n3−2n as an ion-associate [38].
According to the literature, the formation of ion-associates in solution does not lead to changes in its conductivity. Ion pairing or association occurs when oppositely charged ions are closer than a certain critical distance. They then can act as a neutral form and hence do not contribute to conductivity [34,39].
Based on the above, determining the type of soluble REM form in a carbonate-ion medium facilitates the development of approaches for their subsequent extraction and separation from the productive solution. Therefore, the aim of this study was to establish the feasibility of REM ion-associates existing in the Ln3⁺—CO32−—H2O system.

2. Materials and Methods

Measuring the specific electrical conductivity (SEC) of the system formed during the dissolution of synthetic REM (III) carbonates in a potassium carbonate medium facilitated confirming or refuting the presence of associates.
The use of Ln2(CO3)3 as the material for conductometric studies eliminated the influence of foreign anions and/or added water on SEC values. The selected concentration of the potassium carbonate solution, 3 mol/L, corresponded to the range in which SEC increases with concentration (Figure 2) and remained within the sensitivity limits of the device («Anion 4100»). The main technical characteristics of «Anion 4100» are its measurement range of SEC from 10−6 S/cm to 10−1 S/cm and that its limit of permissible basic relative SEC measurement error of solutions is no more than 2%.
This study of the effect of potassium, sodium, and ammonium cations on REM carbonate solubility in 0.5–3 M of carbonate ion medium was undertaken using cerium carbonate as an example under standard conditions and a liquid-to-solid ratio of 2000 mL/g (Figure 3).
The main laboratory equipment for all declared experiments was a HEL Automate II Parallel Reactor System (H.E.L. Group, London, UK) fitted with temperature and stirring speed sensors. Thus, the mixtures’ mixing was organized thermostatically.
This series of experiments was conducted under standard conditions by mixing solid REM (III) carbonate with a potassium carbonate solution at solid-to-liquid ratios from 1:2000 g/mL to 1:40 g/mL. Each experiment was carried out for 12 h with stirring at 200 rpm to reach an equilibrium characterized by the complete dissolution of the precipitate.
Another potential method for identifying the soluble forms of REMs is monitoring the reduction in carbonate ion concentration after the complexation process. When a complex ion, Ln(CO3)n3−2n, is formed via covalent bonds, a decrease in CO32⁻ concentration does not lead to its decay due to the relatively high stability constants. In contrast, the presence of ion-associates would result in their decomposition, as ion pairs and other associates are prone to it [40]. As among soluble carbonates only ammonium carbonate tends to decompose at temperatures below the boiling point of the solution (60–70 °C), the reduction in concentration due to thermal decomposition was studied in this medium. In this series of experiments, solutions of REM nitrate (0.4 mol/L) and ammonium carbonate (3 M) were mixed during 5–10 min at a volume ratio of 1:20 mL/mL. After precipitation and subsequent dissolution, the solution was heated to 70–75 °C. The secondary precipitate formed during ammonium carbonate decomposition was quantified using a gravimetric method, while the REM concentration in the final solution was determined via complexometric titration with Trilon B in the presence of Arsenazo (III) using Equation (3):
C L n = C T B × V T B V L n
where C L n —normal concentration of REM (III), eq/L; V L n —volume of the aliquot, L; C T B —normal concentration of Trilon B (III), eq/L; and V T B —volume of the titrant, L.
Among the possible insoluble REM (III) compounds that could form upon the decay of the ion-associate, only Ln2(CO3)3 was considered. For precipitates obtained, identification was determined via SEM-EDX analysis by scanning electron microscope VEGA 3 LMH with an energy dispersive X-ray microanalysis system (TESCAN Essence, Brno, Czech Republic). Thus, the REM carbonate yield can be calculated using Equation (4):
η L n 2 ( C O 3 ) 3 = m L n 2 ( C O 3 ) 3 p m L n 2 ( C O 3 ) 3 t × 100 % = m L n 2 ( C O 3 ) 3 p × 2 C L n ( N O 3 ) 3 × V L n ( N O 3 ) 3 × M L n 2 ( C O 3 ) 3 × 100 %
where η L n 2 ( C O 3 ) 3 —yield of Ln2(CO3)3, %; m L n 2 ( C O 3 ) 3 p —the mass of Ln2(CO3)3 after drying, g; m L n 2 ( C O 3 ) 3 t —stoichiometrically calculated mass of Ln2(CO3)3, g; C L n ( N O 3 ) 3 —the concentration of the Ln(NO3)3, solution, mol/L; V L n ( N O 3 ) 3 —the volume of the Ln(NO3)3, solution, L; and M L n 2 ( C O 3 ) 3 —the molar mass of Ln2(CO3)3.
The concentration of ammonium carbonate in the final solution was determined using conductometric titration with sodium hydroxide.
A short thermodynamic assessment of performed processes was completed. The Gibbs energy change during these reactions to REM carbonates obtained through its ion-associates was estimated by applying the Hess law. A database of the Chemistry Faculty of Moscow State University «https://www.chem.msu.ru/cgi-bin/tkv.pl» (accessed on 17 February 2025) was chiefly used for this purpose.

3. Results

The experimentally determined SEC of the aqueous potassium carbonate solution at 25 °C was 263.2 mS/cm. Upon adding a sample of thulium (III) carbonate to this solution at solid-to-liquid ratios of 1:2000 g/mL, 1:100 g/mL, and 1:40 g/mL, the electrical conductivity of the system decreased, reaching a minimum 2 min after mixing. The conductivity values were 259.1 mS/cm, 253.1 mS/cm, and 252.2 mS/cm, respectively. Whereafter, they gradually returned to the initial conductivity value of 263.2 mS/cm by 4, 6, and 9 min (Figure 4).
The yields of REM (III) carbonates were calculated after heating the solutions that contained the rare earth metals (III) ion-associates for 60, 120, and 240 min (Figure 5), as follows:
  • Yield of Ln2(CO3)3 after 60 min: La—98.8 %; Nd—98.3 %; Pr—99.6 %; Sm—97.9 %; Tb—99.4 %; Dy—87.2 %; Ho—63.3 %; Y (Er)—51.6 %; Tm—0 %; Lu—0 %.
  • Yield of Ln2(CO3)3 after 120 min: La—98.8 %; Nd—98.3 %; Pr—99.6 %; Sm—97.9 %; Tb—99.4 %; Dy—98.4 %; Ho—74.5 %; Y (Er)—60.9 %; Tm—5 %; Lu—5 %.
  • Yield of Ln2(CO3)3 at 240 min reached approximately 100 %, including Tm and Lu.
The kinetics of ammonium carbonate decomposition were studied using a model solution (initial concentration 3 mol/L) at a temperature of 70–75 °C over a period of 3 h. Based on data shown in Figure 6, the concentration of (NH4)2CO3 decreased from 3 mol/L to 1.9 mol/L after 1 h, and from 3 mol/L to 1.05 mol/L after 2 h.
The results of SEM-EDX analysis of precipitates produced in the process of REM ion-associates decay are illustrated in Figure 7 and Figure 8 using thulium precipitate as an example. The thulium precipitate was composed of 71.48 wt. % thulium (Tm), 23.63 wt. % oxygen (O), and 4.89 wt. % carbon (C).
Preliminary experiments in the field of REM leaching from technogenic phosphogypsum were carried out. Leaching was organized by a 4 M carbonate solution that was stirred for 3 h at a temperature of 90 °C and an L:S 100 mL per 1 g of PG. The degrees of extraction were as follows: La—40.1%, Ce—58.2%, Nd—62.5%, Dy—64.0%, Er—66.4%, Y—72.9%, and Yb—76.8%.

4. Discussion

The difference in cerium (III) carbonate solubility in potassium, sodium, and ammonium carbonate medium indicates the influence of the cation nature, which is characteristic of the association process.
The initial change in electrical conductivity, as shown in Figure 4, was caused by the formation of a suspension, with a higher amount of added powder (such as 0.1 g, 2 g, and 5 g) leading to a greater drop in the conductivity of the solution. After 2 min, an increase in specific electrical conductivity was observed, accompanied by the dissolution of Tm2(CO3)3. Complete dissolution of the precipitate, depending on the solid-to-liquid ratio, was observed within 5–10 min. Complete dissolution of the precipitate was characterized by the return to the initial SEC value (263.2 mS/cm) for all considered phase ratios, confirming the formation of a thulium carbonate complex in the form of an ion-associate.
The behavior of carbonate complexes of light REEs (lanthanum and neodymium), medium-mass REEs (samarium and gadolinium), and heavy REEs (terbium, dysprosium, holmium, thulium, and yttrium) varied with a decrease in carbonate ion concentration. When heating solutions containing La (III), Nd (III), and Sm (III) at 70–75 °C, turbidity was observed at 15 min into the decomposition of ammonium carbonate, accompanied by the formation of the corresponding REE (III) carbonates. For Tb (III) and Dy (III), precipitation began at 20 min, for Ho (III) it began at 35 min, for Y at 40 min, for Tm at 110 min, and for Lu at 120 min.
According to the SEM-EDX analysis results, there was a possibility of the REM carbonate formation, or a like compound, in the ion-associate decay process. In a thulium carbonate, a mass fraction must be 65.24 wt. %, but it was in fact 71.48 wt. %. Therefore, the excursion was in the area of 6 wt. %
The tendency of REM carbonate complexes to decompose, forming a secondary precipitate such as Ln2(CO3)3 upon a decrease in CO32⁻ concentration, serves as additional evidence that the soluble forms of Ln(III) in concentrated solutions of (NH4)2CO3, K2CO3, or Na2CO3 are ion-associates.
Carbonate ion concentration decreases led to a chemical equilibrium shift towards the formation of REM carbonates. Moreover, the difference in the time required for the disintegration of ion-associates can be explained by the difference in individual elements’ stability constants; i.e., a higher value of the stability constant required longer heating for a significant decrease in the carbonate ion in the solution.
The variation in the time required for the decay of ion-associates was due to differences in the strength of electrostatic attraction between anions and individual groups of REMs (III). Ions with a higher charge and smaller size exhibit stronger electrostatic interactions [40]. Therefore, the shorter decay times of light and medium REM associates resulted from their lower stability, indirectly suggesting a predominance of loose associates. In contrast, the strong associates formed by heavy REMs were primarily characterized as close (contact) associates.
The concentration of (NH4)2CO3 in the productive solution after the decay of ion-associates was assumed to be according to Figure 6. An example of the material balance is presented in Table 2, characterizing the decay process of the terbium (III) ion-associate during heating for 1 h.
The material balance accounts for the processes described by Equations (8) and (12), which are end-to-end, and consist of Equations (5)–(11).
Precipitation :   2 L n ( a q ) 3 + + 3 C O 3 ( a q ) 2 L n 2 ( C O 3 ) 3 ( s )
Ion-association  ( dissolution ) :   L n 2 ( C O 3 ) 3 s + C O 3 a q 2 2 L n ( C O 3 ) 2 ( a q )
Decay   of  ion-associates :   2 L n ( C O 3 ) 2 a q L n 2 ( C O 3 ) 3 s + C O 3 a q 2
End-to-end  equation :   2 L n ( a q ) 3 + + 3 C O 3 ( a q ) 2 L n 2 ( C O 3 ) 3 ( s )
Hydrolysis :   2 N H 4 ( a q ) + + C O 3 a q 2 + 2 H 2 O ( l ) 2 N H 3 · H 2 O l + H 2 C O 3 ( l )
Decomposition :   H 2 C O 3 ( l ) C O 2 g + H 2 O ( l )
Decomposition :   N H 3 · H 2 O l N H 3 g + H 2 O ( l )
End-to-end  equation :   2 N H 4 ( a q ) + + C O 3 a q 2 2 N H 3 g + C O 2 g + H 2 O ( l )
Figure 9 shows the calculated values of Gibbs energy for mono- and di-carbonate REM complexes in carbonate–carbonate systems. Similar values were obtained when REM sulfates and phosphates were leached by carbonate solution [41]. Therefore, complexation processes are possible.
If Ln is Tb, the Gibbs energy change at standard conditions during these processes as ΔG° (5) or (8) = −2.27 kJ/mol, ΔG° (6) −160 kJ/mol, and ΔG° (7) = 149.46 kJ/mol. The reactions from (9) to (12) are characterized as follows: ΔG° (9) = 230.70 kJ/mol, ΔG° (10) = −104.02 kJ/mol, ΔG° (11) = 0.28 kJ/mol, and ΔG° (12) = 127.24 kJ/mol.
On one hand, a positive value of ion-associate decay (7) reflects a theoretical stability of the complex compound. However, on the other hand, a carbonate ion decrease and its subsequent removal from the system lead to an equilibrium shift towards the REM carbonates’ formation. This can be explained either by the formation of intermediate compounds or by complexation as an ion-association without strong covalent bonds.
Based on the analysis of the temperature effect at 60–75 °C on the decay of ion-associates (due to the decrease in ammonium carbonate concentration), the formation of rare earth metal (III) carbonates up to terbium occurred in a shorter time (τ2) and with a higher yield compared to heavier rare earth metals, whose ion-associates decayed over a longer time (τ1). Thus, the mechanism for the formation of rare earth metal (III) carbonates can be characterized by the scheme shown in Figure 10.

5. Conclusions

These experimental findings confirm the existence of complex compounds of rare earth metals in the form of ion-associates within a high-concentration carbonate-ion medium (3 mol/L). The strength of electrostatic attraction between REM (III) ions and carbonate anions systematically increased from the light to the heavy REM group, which directly influenced the stability of the resulting associates. Ion-associates of light REMs and medium-mass REMs (up to terbium) were predominantly characterized as loose, whereas those formed by metals beyond terbium were more likely to be contact associates. Variations in the time required for REM (III) carbonates to precipitate resulted in distinct concentration thresholds for different REM groups. These observations suggest that during the carbonate–alkaline processing of primary or secondary REM sources into REM (III) carbonates, the formation of ion-associates as intermediate products may facilitate group separation of REMs through selective precipitation.
Particularly, phosphogypsum processing by the carbonate method should involve treatment of the solid phase by ammonium carbonate exclusively or a mixed ammonium and potassium (sodium) carbonates solution, depending on the REM content in the material. Because the vast majority of technogenic PG includes predominantly light REMs, the second variant would be more prospective. In this case, REM ion-associates needed insignificant carbonate ion decrease for decay into REM carbonates.

Author Contributions

Conceptualization, T.L. and S.G.; methodology, T.L.; software, V.S.; validation, V.S. and E.L.; formal analysis, S.G. and E.L.; investigation, S.G.; resources, V.S.; data curation, T.L.; writing—original draft preparation, S.G.; writing—review and editing, T.L. and S.G.; visualization, V.S.; supervision, T.L.; project administration, S.G. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Data Availability Statement

The original contributions presented in this study are included in the article. Further inquiries can be directed to the corresponding author.

Conflicts of Interest

The authors declare no conflicts of interest.

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Figure 1. Mechanism of contact (close) ion pair formation [33].
Figure 1. Mechanism of contact (close) ion pair formation [33].
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Figure 2. Dependence of solution-specific electrical conductivity on K2CO3 concentration at 25 °C.
Figure 2. Dependence of solution-specific electrical conductivity on K2CO3 concentration at 25 °C.
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Figure 3. Influence of carbonate ion concentration on cerium (III) carbonate solubility at 25 °C.
Figure 3. Influence of carbonate ion concentration on cerium (III) carbonate solubility at 25 °C.
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Figure 4. Change in specific electrical conductivity upon adding Tm2(CO3)3 to K2CO3 solution.
Figure 4. Change in specific electrical conductivity upon adding Tm2(CO3)3 to K2CO3 solution.
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Figure 5. Yield of Ln2(CO3)3 upon decay of ion-associates.
Figure 5. Yield of Ln2(CO3)3 upon decay of ion-associates.
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Figure 6. Kinetics of (NH4)2CO3 decomposition.
Figure 6. Kinetics of (NH4)2CO3 decomposition.
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Figure 7. SEM image of thulium precipitate during its ion-associate decay.
Figure 7. SEM image of thulium precipitate during its ion-associate decay.
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Figure 8. SEM-EDX mapping of thulium precipitate during its ion-associate decay.
Figure 8. SEM-EDX mapping of thulium precipitate during its ion-associate decay.
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Figure 9. Gibbs energy changes during rare earth metal (III) carbonates’ dissolution in carbonate-ion medium.
Figure 9. Gibbs energy changes during rare earth metal (III) carbonates’ dissolution in carbonate-ion medium.
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Figure 10. Mechanism of formation of rare earth metal (III) carbonates under atmospheric pressure.
Figure 10. Mechanism of formation of rare earth metal (III) carbonates under atmospheric pressure.
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Table 1. Stability constants of REM carbonate complexes [32].
Table 1. Stability constants of REM carbonate complexes [32].
REMOhta and KawabeLiu and BurneREMOhta and KawabeLiu and Burne
lgK1lgK2lgK1lgK2lgK1lgK2lgK1lgK2
La8.3312.526.5211.58Dy8.9514.387.3313.18
Ce8.5813.066.8612.05Ho8.9614.487.3213.27
Pr8.7313.437.0312.37Er9.0214.627.3813.39
Nd8.7513.597.0812.46Tm9.1014.797.4513.54
Sm8.9013.957.2512.82Yb9.1514.947.5813.56
Eu8.8614.027.2612.91Lu9.1314.967.5313.64
Gd8.7813.957.1712.76Y8.8814.297.2512.90
Tb8.8814.227.2313.05Sc-17.41--
Table 2. Material balance of process for terbium carbonate formation.
Table 2. Material balance of process for terbium carbonate formation.
InputOutput
ItemMass, gItemMass, g
1Ammonium carbonate solution:219.401Productive solution:199.00
Ammonium carbonate57.60Ammonium carbonate34.10
Water161.80Ammonium nitrate0.96
2Terbium nitrate (III) solution:11.18Water163.94
Terbium nitrate (III)1.382Water11.06
Water9.8Water (evaporation)6.55
Total:230.58Water from Equation (5)4.51
3Ammonia8.51
4Carbon dioxide11.02
5Terbium carbonate (III)0.99
Total:230.58
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Litvinova, T.; Gerasev, S.; Sergeev, V.; Lidanovskiy, E. Rare Earth Metal Ion-Associates in Ln3+—CO32−—H2O System. Metals 2025, 15, 239. https://doi.org/10.3390/met15030239

AMA Style

Litvinova T, Gerasev S, Sergeev V, Lidanovskiy E. Rare Earth Metal Ion-Associates in Ln3+—CO32−—H2O System. Metals. 2025; 15(3):239. https://doi.org/10.3390/met15030239

Chicago/Turabian Style

Litvinova, Tatiana, Stepan Gerasev, Vasiliy Sergeev, and Egor Lidanovskiy. 2025. "Rare Earth Metal Ion-Associates in Ln3+—CO32−—H2O System" Metals 15, no. 3: 239. https://doi.org/10.3390/met15030239

APA Style

Litvinova, T., Gerasev, S., Sergeev, V., & Lidanovskiy, E. (2025). Rare Earth Metal Ion-Associates in Ln3+—CO32−—H2O System. Metals, 15(3), 239. https://doi.org/10.3390/met15030239

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