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Model studies on granular activated carbon adsorption in fixed bed filtration
A B Jusoh1, M J M M Noor, S B Plow
1Faculty of Science & Technology, Kolej Universiti Sains & Teknologi Malaysia, Kuala Terengganu.
Summary
This study investigated natural organic matter (NOM) removal using granular activated carbon (GAC) filters. The Clark model effectively simulated NOM adsorption, with lower empty bed contact times yielding better results for GAC filtration.
Area of Science:
- Environmental Science
- Water Treatment Engineering
- Adsorption Science
Background:
- Natural organic matter (NOM) removal is crucial for water purification.
- Granular activated carbon (GAC) is a common adsorbent for NOM.
- Understanding adsorption kinetics and modeling is essential for optimizing GAC performance.
Purpose of the Study:
- To evaluate the efficiency of GAC in removing NOM from water.
- To compare the performance of different GAC materials (KI-6070 and KI-8085).
- To assess the applicability of various adsorption models (Adams-Bohart, Bed-Depth-Service-Time, Clark) for NOM removal.
Main Methods:
- Continuous flow fixed bed column experiments were conducted.
- Two types of GAC with different surface areas were utilized.
- Adsorption data were fitted using Adams-Bohart, Bed-Depth-Service-Time, and Clark models.
- The impact of empty bed contact time (EBCT) on adsorption was investigated.
Main Results:
- Adsorption of NOM onto GAC was a complex process involving multiple rate-limiting steps.
- Critical bed depths for KI-6070 and KI-8085 were determined to be 0.24 m and 0.3 m, respectively.
- The Clark model provided a better simulation of the adsorption breakthrough process compared to the Adams-Bohart model.
- Shorter EBCT (15 minutes) showed a better fit with the Clark Model.
Conclusions:
- GAC is effective for NOM removal, but the process is complex.
- The Clark model is a suitable tool for simulating GAC adsorption of NOM.
- Optimizing EBCT is important for enhancing the predictive accuracy of adsorption models and improving GAC filtration efficiency.