Kinetic, equilibrium and selectivity studies of heavy metal ions (Pb(II), Co(II), Cu(II), Mn(II), and Zn(II)) removal from water using synthesized C-4-methoxyphenylcalix[4]resorcinarene adsorbent. Issue 10 (25th February 2016)

• Record Type: Journal Article
• Authors: Alshahateet, Solhe F.; Jiries, Anwar G.; Al-Trawneh, Salah A.; Eldouhaibi, Ahmad S.; Al-Mahadeen, Mohammed M.
• Is Part Of: Desalination and water treatment. Volume 57:Issue 10(2016)
• Page Start: 4512
• Page End: 4522
• Publication Date: 2016-02-25
• Subjects: Adsorption -- Synthetic adsorbent -- Atomic Absorption Spectroscopy -- Adsorption selectivity -- C-4-Methoxyphenylcalix[4]resorcinarene -- Cu(II) -- Mn(II) -- Zn(II) -- Pb(II) -- Co(II); Saline water conversion -- Periodicals; Saline water conversion; Water -- Purification; Periodicals; 628.167
• DOI: 10.1080/19443994.2014.991762
• Languages: English
• ISSNs: 1944-3994

Abstract

Abstract: Batch-mode adsorption study was done for selected heavy metal ions (Pb(II), Co(II), Cu(II), Mn(II), and Zn(II)) using synthetic adsorbent ( C -4-methoxyphenylcalix[4]resorcinarene3 ) to investigate the effect of different parameters such as contact time and pH. Selectivity of the adsorbent towards a mixture of heavy metals adsorbates was investigated. Results showed optimum agitation time of 30 min at pH 5.6 and initial concentration of 1 ppm for all investigated heavy metals. Different kinetic models of Santosa first-order, Lagergren pseudo-first-order and Ho pseudo-second-order were applied on the adsorption experimental data. Results proved that all adsorption processes were followed and pseudo-second-order kinetic model was adopted. The adsorption capacity of C -4-methoxyphenylcalix[4]resorcinarene towards the selected heavy metal ions was 95.00, 89.76, 89.58, 86.43, and 80.96% for Cu(II), Mn(II), Zn(II), Pb(II), and Co(II), respectively. Selectivity of adsorption was tested on a mixture of Cu(II), Mn(II), Zn(II), Pb(II), and Co(II) with an initial concentration of 1 ppm of each heavy metal and agitated time of 10 min with the adsorbent; removal percentage of each metal ion showed different values from each heavy metal alone as it was in decreasing order Cu(II) > Zn(II) > Co(II) > Mn(II) > Pb(II). The rate constant value for each heavy metal adsorption mechanism obtained from Ho pseudo-second-order model was in the order Co(II) > Zn(II) > Pb(II) > Mn(II) > Cu(II).