Dergiler / Sakarya University Journal of Science / 2020 / Cilt: 24 Sayı: 5

Modelling of Remazol Black-B adsorption on chemically modified waste orange peel: pH shifting effect of acidic treatment

Sayfa
1135–1150
Yayın Tarihi
2020-10-01
DOI
—
🏛️Bu makalenin bibliyografik verileri ve tam metin bağlantısı DergiPark üzerinden sağlanmıştır.
DergiPark Kaydı ↗
✨

Yapay Zeka Hızlı Bakış & Çıkarımlar

AI Insight
⚡ TL;DR(1 Cümlede Hızlı Çıkarım)

These parameters were calculated as -4.24 kJ.mol-1, 43.77 kJ.mol-1, 0.16 kJ mol-1.K-1 for CMOP respectively whereas for DOP -3.58 kJ.mol-1,-19.79 kJ.mol-1, -0.05 kJ mol-1.K-1 .

📌 3 Maddede Bu Makale

🎯
Amaç & Hipotez:The adsorption of Remazol Black-B (RBB) onto two different types of agricultural waste derived-adsorbents; dried-orange peel (DOP) and chemically modified orange peel (CMOP), was performed.
📊
Temel Bulgular & Veri:The adsorption rate, capacity, and the dye removal efficiency were investigated in terms of initial pH ranged between 2.0 to 10.0 of the dispersion and the operating temperature of 25 °C, 35 °C, 45 °C .
💡
Sonuç & Katkı:These parameters were calculated as -4.24 kJ.mol-1, 43.77 kJ.mol-1, 0.16 kJ mol-1.K-1 for CMOP respectively whereas for DOP -3.58 kJ.mol-1,-19.79 kJ.mol-1, -0.05 kJ mol-1.K-1 .
🔬Tür:Modelleme & Sayısal Simülasyon
📍Kapsam:Genişletilmiş Akademik Örneklem
⚙️Değişkenler:Adsorption · Orange Peel · Remazol Black-B

Abstract

The adsorption of Remazol Black-B (RBB) onto two different types of agricultural waste derived-adsorbents; dried-orange peel (DOP) and chemically modified orange peel (CMOP), was performed. The adsorption rate, capacity, and the dye removal efficiency were investigated in terms of initial pH ranged between 2.0 to 10.0 of the dispersion and the operating temperature of 25 °C, 35 °C, 45 °C . The Langmuir and Freundlich adsorption models were applied to the experimental data to model the adsorption equilibrium, and evaluated by regression analysis. The results indicated that the Langmuir model was more suitable to describe the adsorption equilibrium of RBB over CMOP. According to Langmuir model, while the highest RBB uptake capacity of DOP was determined as 62.4 mg.g-1 at pH 2.0 and 25°C, this value was figured out for CMOP as 84.4 mg.g-1 at pH 8.0 and 45°C. Furthermore, the adsorption kinetics followed both the pseudo-second order and the saturation type kinetic models for each adsorbent-dye system. The thermodynamic parameters of adsorption including the Gibbs free energy change (ΔGo), the enthalpy change (ΔHo), and the entropy change (ΔSo) were obtained by using thermodynamic equations. These parameters were calculated as -4.24 kJ.mol-1, 43.77 kJ.mol-1, 0.16 kJ mol-1.K-1 for CMOP respectively whereas for DOP -3.58 kJ.mol-1,-19.79 kJ.mol-1, -0.05 kJ mol-1.K-1 .

🔖

Bu Makaleye Atıf Yap

KARAMAN, C., AKSU, Z. (2020). Modelling of Remazol Black-B adsorption on chemically modified waste orange peel: pH shifting effect of acidic treatment. Sakarya University Journal of Science, Cilt: 24 Sayı: 5, 1135–1150. https://ajindex.com/articles/941894

📄 Tam Metin PDF Okuyucu

📄

PDF görüntüleyici hazırlanıyor...

Kaynakça (6)

  1. S.P. Kodal and Z. Aksu, "Cationic surfactant-modified biosorption of anionic dyes by dried Rhizopus arrhizus." Environmental technology, vol. 38, no. 20, pp. 2551-2561, 2017. Z. Aksu, “Application of biosorption for the removal of organic pollutants: a review.” Process Biochemistry, vol. 40, pp. 997−1026, 2005. E. Bayram and E. Ayranci, “Investigation of changes in properties of activated carbon cloth upon polarization and of electrosorption of the dye basic blue-7.” Carbon, vol. 48, pp. 1718–1730, 2010.
  2. S.P.D Monte Blanco, F.B. Scheufele, A.N. Modenes, F.R. Espinoza-Quinones, P. Marin, A.D. Kroumov and C.E. Borba, “Kinetic, equilibrium and thermodynamic phenomenological modeling of reactive dye adsorption onto polymeric adsorbent.” Chemical Engineering Journal, vol. 307, pp. 466-475, 2017. Z. Aksu and A. İsoglu, “Use of agricultural waste sugar beet pulp for the removal of Gemazol turquoise blue-G reactive dye from aqueous solution.” Journal of Hazardous Materials B, vol. 137, pp. 418-430, 2006.
  3. A.A. Attia, B.S. Girgis, and N.A. Fathy, “Removal of methylene blue by carbons derived from peach stones by H3PO4 activation: batch and column studies.” Dyes and Pigments, vol. 76, pp. 282–289, 2008. M, Olivares-Marín, C. Fernández-González A. Macías-García, and V. Gómez-Serrano, “Preparation of activated carbons from cherry stones by activation with potassium hydroxide.” Applied Surface Science, vol. 252,pp. 5980–5983, 2006.
  4. W. Li, K. Yang, J. Peng, L. Zhang, S. Guo, and H. Xia, “Effects of carbonization temperatures on characteristics of porosity in coconut shell chars and activated carbons derived from carbonized coconut shell chars.” Industrial Crops and Products, vol. 28, pp. 190–198, 2008.
  5. I.A.W. Tan, A.L. Ahmad, and B.H. Hameed, “Adsorption of basic dye on high-surface-area activated carbon prepared from coconut husk: equilibrium, kinetic and thermodynamic studies.” Journal of Hazardous Materials, vol. 154, pp. 337–346, 2008.
  6. F.S. Vieira, A.R. Cestari, I.F. Gimenez, N.L.V. Carreño, and L.S. Barreto, “Kinetic and calorimetric study of the adsorption of dyes on mesoporous activated carbon prepared from coconut coir dust.”Journal of Colloid and Interface Science, vol. 298, pp. 515–522, 2006. M. Olivares-Marín, V. Del-Prete, E. Garcia-Moruno, C. Fernández-González, A. Macías-García, and V. Gómez-Serrano, “The development of 500 an activated carbon from cherry stones and its use in the removal of ochratoxin A from red wine.” Food Control. vol. 20, no. 3, pp. 298