Synthesis of β-Tricalcium Phosphate/PEG 6000 Composite by Novel Dissolution/Precipitation Method: Optimization of the Adsorption Process Using a Factorial Design-DFT and Molecular Dynamic

被引:21
作者
Azzaoui, K. [1 ]
Aaddouz, M. [2 ]
Akartasse, N. [2 ]
Mejdoubi, E. [2 ]
Jodeh, S. [3 ]
Hammouti, B. [8 ]
Taleb, M. [1 ]
ES-Sehli, S. [1 ]
Berisha, A. [4 ]
Rhazi, L. [5 ]
Lamhamdi, A. [6 ]
Algarra, M. [7 ]
机构
[1] Sidi Mohamed Ben Abdellah Univ, Lab Engn Electrochem Modeling & Environm, Fac Sci, Fes 30000, Morocco
[2] Mohammed First Univ, Fac Sci, Lab Appl Chem & Environm, Oujda 60000, Morocco
[3] An Najah Natl Univ, Dept Chem, POB 7, Nablus, Palestine
[4] Univ Prishtina, Fac Nat & Math Sci, Dept Chem, Prishtina 10000, Kosovo
[5] Univ Artois, Inst Polytech UniLaSalle, ULR 7519, 19 Rue Pierre Waguet, BP 30313, F-60026 Beauvais, France
[6] Abdelmalek Essaadi Univ, Natl Sch Appl Sci ENSAH, Lab Appl Sci, Tetouan, Morocco
[7] Univ Publ Navarra, INAMAT2 Inst Adv Mat & Math, Dept Sci, Campus Arrosadia, Pamplona 31006, Spain
[8] Euro Mediterranean Univ Fes, BP 15, Fes 30070, Morocco
关键词
Adsorption; Composite; beta-Tricalcium phosphate; PEG; 6000; Lead (II); Molecular dynamic; THERMAL VAPOR COMPRESSION; MULTIEFFECT DESALINATION SYSTEM; STEADY-STATE ANALYSIS; MED-TVC PLANT; THERMOECONOMIC ANALYSIS; PERFORMANCE ANALYSIS; DISTILLATION SYSTEM; WASTE HEAT; FEED; EXERGY;
D O I
10.1007/s13369-023-08390-8
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
We propose the synthesis of a tricalcium phosphate and PEG 6000 composite for use in the removal of dangerous metal ions from wastewater using a unique method of synthesis dissolution precipitation. The efficiency of the composite's adsorption toward Pb2+ and other harmful metal ions found in sewage was evaluated using FTIR, XRD, and SEM composite analysis as a function of adsorbent dose, temperature, pH, time, and starting metal ion. According to the experimentally determined results, the pseudo-second order's value of R-2 (0.914-0.943) is larger than the pseudo-first-order's (0.913-0.968) on the beta-TCP and beta-TCP-PEG 6000, respectively. The calculated q(e) values (12.592-12.452 mg/g) are reasonably close to the measured q(e) values for TCP and TCP-PEG 6000, which range from 90.160 to 100.736 mg/g. Thermodynamic findings support the spontaneous metal attachment to the composite's receptor regions. The results of the DFT show that the Pb2+ ion has a significant interaction with the TCP/PEG6000 surface. This is the case even though the Pb2+ ions are far smaller than the TCP/PEG 6000 molecule. The results presented here are supported by evidence acquired from experiments. The novelty of this study is, tricalcium phosphate (TCP) has a crystalline structure and is composed of calcium ions (Ca2+) and phosphate ions (PO43-). In the TCP crystal structure, the calcium ions occupy the hexagonal layers, and the phosphate ions occupy the tetrahedral interstitial sites between the hexagonal layers. The TCP crystal structure can accommodate substitutions of calcium or phosphate ions with other ions, which can lead to variations in its properties and applications.
引用
收藏
页码:711 / 732
页数:22
相关论文
共 55 条
[1]  
Abdelbasit Khalid, 2015, Water Desalination Through Thermal Systems-MED Technology
[2]   Exergoeconomic optimization of a forward feed multi-effect desalination system with and without energy recovery [J].
Abid, Asad ;
Jamil, Muhammad Ahmad ;
Sabah, Noor Us ;
Farooq, Muhammad Umer ;
Yaqoob, Haseeb ;
Khan, Liaquat Ali ;
Shahzad, Muhammad Wakil .
DESALINATION, 2021, 499
[3]   A multi-objective optimisation framework for MED-TVC seawater desalination process based on particle swarm optimisation [J].
Al-hotmani, O. M. A. ;
Al-Obaidi, M. A. ;
Li, J. P. ;
John, Y. M. ;
Patel, R. ;
Mujtaba, I. M. .
DESALINATION, 2022, 525
[4]   Optimisation of multi effect distillation based desalination system for minimum production cost for freshwater [J].
Al-hotmani, O. M. A. ;
Al-Obaidi, M. A. ;
Filippini, G. ;
Manenti, F. ;
Patel, R. ;
Mujtaba, I. M. .
29TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PT A, 2019, 46 :169-174
[5]  
Al-Jabr H.A., 2018, EWAS3 2018, V2, P612, DOI DOI 10.3390/PROCEEDINGS2110612
[6]  
Al-Khalifah H., 2022, ENERGY AM SOC MECH E, V6, DOI [10.1115/IMECE2022-96683, DOI 10.1115/IMECE2022-96683]
[7]  
Al-Mutaz IS, 2016, DESALIN WATER TREAT, V57, P26562, DOI [10.1080/19443994.2016.1213482, 10.1080/19443994.2014.910841]
[8]   Parametric simulation of MED-TVC units in operation [J].
Alamolhoda, F. ;
KouhiKamali, R. ;
Asgari, M. .
DESALINATION AND WATER TREATMENT, 2016, 57 (22) :10232-10245
[9]   Cost analysis of multiple effect evaporation and membrane distillation hybrid desalination system [J].
Ali, Emad ;
Orfi, Jamel ;
AlAnsary, Hany ;
Soukane, Sofiane ;
Elcik, Harun ;
Alpatova, Alla ;
Ghaffour, Noreddine .
DESALINATION, 2021, 517
[10]   Steady state analysis of the Tripoli West LT-HT-MED plant [J].
Ashour, MM .
DESALINATION, 2003, 152 (1-3) :191-194