Kinetic, Equilibrium and Selectivity Studies of Heavy Metals (Pb2+, Co2+, Cu2+, Mn2+ and Zn2+)‎ Removal from Aqueous Phase using C-4-substitutedphenylcalix(4)‎ resorcinarenes as Adsorbent Surfaces

العناوين الأخرى

دراسة حركية واتزان و انتقائية عملية إزالة لأيونات العناصر الثقيلة الرصاص (II)‎, الكوبالت (II)‎, النحاس (II)‎, المنغنيز (II)‎ و الزنك (II)‎ من الوسط المائي باستخدام C-4-substitutedphenylcalix[4]resorcinarenes كسطوح ادمصاصية

مقدم أطروحة جامعية

al-Mahadin, Muhammad Musa

مشرف أطروحة جامعية

Jiryis, Anwar Jurj
al-Shahatit, Sulhi Faysal

أعضاء اللجنة

Isa, Ayman Abd Allah
al-Tawil, Samir Ahmad
al-Tarawinah, Salah Abd al-Rahman

الجامعة

جامعة مؤتة

الكلية

كلية العلوم

القسم الأكاديمي

قسم الكيمياء

دولة الجامعة

الأردن

الدرجة العلمية

ماجستير

تاريخ الدرجة العلمية

2014

الملخص الإنجليزي

This thesis is concerned with the re-preparation of C-4-chloropheny-calix[4]resorcinarene, C-4-bromophenylcalix[4]resorcinarene and C-4-methoxyphenylcalix[4]resorcinarene through the acid-catalyzed condensation of resorcinol with the following 4-substitutedbenzaldehydes: 4-chloro-benzaldehyde, 4-bromobenzaldehyde, and 4-methoxybenzaldehyde.

The synthesized compounds were studied as adsorbents for selected heavy metal ions namely Cu(II), Co(II), Zn(II), Mn(II) and Pb(II).

Different adsorption experiments were conducted to determine the optimum adsorption conditions such as pH and contact time.

In addition, the experiments were conducted to examine different kinetic models against our adsorption data.

Finally, the selectivity of the adsorbents (3a-c) towards a mixture of heavy metal ions adsorbates were studied and discussed.

The optimum pH was found to be 5.6 at contact time of 30 min and an initial concentration of 1 ppm for all selected heavy metal ions using C-4-substitutedphenylcalix[4]resorcinarenes (3a-c) as adsorbents.

Different kinetic models have been applied on the adsorption experimental data such as; Santosa first order, Lagergren pseudo first order and Ho pseudo second order.

Results showed that all adsorption processes were followed and adopted pseudo second order kinetic model.

Equilibrium % removal using compound (3a) was found to be around 84.29%, 79.55%, 78.54%, 77.92%, 75.19% for heavy metal ions; Pb(II), Cu (II), Mn(II), Zn(II) and Co(II), respectively.

Using compound (3b) as adsorbent, the equilibrium % removal was found to be 87.86%, 87.73%, 85.52 %, 82.44 %, 76.35% for heavy metal ions; Pb(II), Cu(II), Zn(II), Mn(II) and Co(II), respectively.

Equilibrium removal percentage was found to be 95%, 89.76%, 89.58%, 86.43%, 80.96% for heavy metal ions; Cu(II), Mn(II) Zn(II), Pb(II) and Co(II), respectively when compound (3c) was used as adsorbent.

When a mixture of Cu(II), Co(II), Zn(II), Mn(II) and Pb(II) ions with initial concentration of 1 ppm was used at shaking time of 10 min, removal percentage was ranked in the order Pb(II) > Cu(II) > Zn(II) > Mn(II) > Co(II) when compound (3a) was the adsorbent; Cu(II) > Co(II) > Mn(II) > Pb(II) > Zn(II) when compound (3b) was the adsorbent and Cu(II) > Zn(II) > Co(II) > Mn(II) > Pb(II) when compound (3c) was the adsorbent

التخصصات الرئيسية

الكيمياء

الموضوعات

• الموارد المائية
• الصرف الصحي
• مياه الصرف الصحي
• المياه

عدد الصفحات

69

قائمة المحتويات

• APA
• MLA
• AMA

لغة النص

الإنجليزية

نوع البيانات

رسائل جامعية

رقم السجل

BIM-560263