NoteA new group contribution method for mineral concentration processes
Introduction
Group contribution models assume that a certain property depends on the sum of the contributions made by structural groups. In this way, it is possible to estimate properties of many systems based on a reduced number of groups that constitute those systems. The primary application of these models is in designing chemical products that have the ability to form molecules based on groups of atoms. Additionally, these models have also been used to design separation processes based on fractional distillation (d’Anterroches and Gani, 2005) and recently to estimate the global recovery of concentration circuits (Sepúlveda et al., 2014). In this last work, a model was presented to estimate the recovery of 1492 circuits, which can incorporate 2–6 process stages, based on 35 process groups. To fit the model, data from 46 circuits were used. In the present work, this model is modified and extended to estimate the recovery of over 274 million concentration circuits, which can incorporate 2–9 concentration stages, based on 143 process groups. To fit the model, 293 concentration circuits were used. In addition to these advantages, the proposed contribution model includes circuit designs used in the process industry, the adjusted values αi and βi do not exhibit inconsistencies, and the model can relate the circuits from the database according to the number of process stages that are used.
Section snippets
Process groups
It is assumed that each concentration stage has two outlet streams: a concentrate and a tail. Fig. 1 shows a general diagram of the considered alternatives. The stages, rougher (R), cleaner1 (C1), cleaner2 (C2), and cleaner3 (C3), are defined as follows. Stage R processes the circuit feed, whose concentrate could be the final product or the feed to stage C1. The concentrate generated by this last stage could be the final product or the feed to stage C2. The concentrate generated in stage C2
Recovery models
To estimate the circuit recovery, two models are proposed, which depend on the recovery values in the rougher stage (Sepúlveda et al., 2014). For high recoveries (0.63–1) and low recoveries (0.1–0.37) in the rougher stage, the following model is proposed:where Rcj is the recovery of species j in the circuit; Λi,j is the contribution of group i; NT is the total number of groups in the circuit; NC is the total number of cleaner stages in the
Fitting the models
The group contribution model was fitted using CONOPT-GAMS. The results are shown in Table 2, Table 3.
The measured absolute error (MAE, Eq. (4)) was used to quantify the difference between the predicted recovery and the recovery obtained by mass balance.where Rci,l is the recovery estimated by using group contributions, Rbi,l is the recovery obtained from the mass balance, N is the number of circuits, and M is the number of cases. Table 4 shows the MAE obtained when
Example and validation
As an example, the recovery of two circuits that are not present in the database used to fit the model is estimated. Consider the circuits shown in Fig. 2, Fig. 3. The circuit of Fig. 2 can be partitioned into the groups [RC1S1], [S1SC11S2], [S2SC11W], [C1PCS21], [SC11CS21S1], and , and the circuit of Fig. 3 can be partitioned into [RC1S1], [C1PCS11], [S1C1W], and [CS11PS1]. Applying Eq. (1) the recoveries for the low and high ranges can be obtained:
Conclusions
A group contribution model is presented in this work, which exhibits improvements with respect to the model by Sepúlveda et al. (2014) because it can estimate the recovery of species for a much greater number of concentration circuits and incorporates circuit designs that are used in industry. The model is based on the fact that the developed contribution model allows establishing relationships according to the number of stages of the circuits from the database, which then allows the circuit
Acknowledgments
Financial support from CONICYT (Fondecyt 1120794), CICITEM (R10C1004) and the Antofagasta Regional Government is gratefully acknowledged.
References (4)
- et al.
Group contribution based process flowsheet synthesis, design and modeling
Fluid Phase Equilib
(2005) - et al.
Separation circuits analysis and design using sensitivity analysis
Comput Aided Chem Eng
(2011)