Optimisation of chemical harvesting of microalgae from fish processing wastewater and economic assessment based on process modelling

Chemical flocculation with bio-based coagulants offers an effective method for harvesting microalgae after wastewater treatment. Nevertheless, limited information exists on how the coagulants affect treated wastewater and microalgae biomass quality, and only a few studies have assessed their economic feasibility in industrial operations. This study optimised microalgae ( Chlorella sorokiniana ) harvesting from fish processing wastewater (FPWW) in laboratory-scale experiments and evaluated the economic performance of coagulation-flocculation-sedimentation process followed by minimal centrifugation (case study 1) versus conventional centrifugation alone (case study 2) using process simulation. Chitosan achieved 97 % harvesting efficiency at 15 mg/L concentration, while tannin coagulant (TC) achieved 98 % at 10 mg/L and was less sensitive to overdosing. TC was further examined for harvesting C. sorokiniana during FPWW treatment. The best performance (94 %) was achieved on day 15 at pH 5 using only 15 mg/L TC. Under these conditions, treated water met wastewater discharge standards for total nitrogen (8.5 mg/L) and total phosphorus (0.4 mg/L), and the biomass obtained high protein content (52.9 %), with minimal impact from TC on its quality. Techno-economic analysis showed that, while centrifugation (case study 2) yielded slightly higher biomass quality, the TC-based harvesting method with minimal centrifugation (case study 1) achieved a reduction of roughly 10 % in operating and annual capital costs. A sensitivity analysis indicated that labour cost, the cost of capital and the electricity price were the key cost drivers for both case studies in the base case scenario. Additionally, scale-up calculations with 10- and 100-fold increases in flow rate showed that case study 1 resulted in more moderate growth in operating and annual capital costs, showing a more economically sustainable option for large-scale microalgae recovery. • Tannin coagulant at 15 mg/L efficiently harvested C. sorokiniana from FPWW at pH 5. • Treated FPWW had TN (8.5 mg/L), TP (0.4 mg/L) and biomass contained 52.9 % protein. • TC-based harvesting had ∼10 % lower base case operating and annual capital costs. • Harvesting cost is driven by labour cost, cost of capital and electricity price. • TC-based harvesting showed lower cost escalation with scale-ups than centrifugation.

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Publication Details

Journal
Chemical Engineering Journal
Published
2025-10-04
DOI
https://doi.org/10.1016/j.cej.2025.169036
Citations
2
Primary Topic
Algal biology and biofuel production
Type
article
Field-Weighted Citation Impact
0.73
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article

Optimisation of chemical harvesting of microalgae from fish processing wastewater and economic assessment based on process modelling

Ulla Moilanen, Ville-Hermanni Sotaniemi, Tiina Leiviskä, Adedayo Bello et al.
2 citations
Chemical Engineering Journal
Algal biology and biofuel production
0.73
article

Optimisation of chemical harvesting of microalgae from fish processing wastewater and economic assessment based on process modelling

Ulla Moilanen, Ville-Hermanni Sotaniemi, Tiina Leiviskä, Adedayo Bello, Saba Khalatbari, Juha Tanskanen, Ville Tuppurainen
article en
2 citations

Abstract

Chemical flocculation with bio-based coagulants offers an effective method for harvesting microalgae after wastewater treatment. Nevertheless, limited information exists on how the coagulants affect treated wastewater and microalgae biomass quality, and only a few studies have assessed their economic feasibility in industrial operations. This study optimised microalgae ( Chlorella sorokiniana ) harvesting from fish processing wastewater (FPWW) in laboratory-scale experiments and evaluated the economic performance of coagulation-flocculation-sedimentation process followed by minimal centrifugation (case study 1) versus conventional centrifugation alone (case study 2) using process simulation. Chitosan achieved 97 % harvesting efficiency at 15 mg/L concentration, while tannin coagulant (TC) achieved 98 % at 10 mg/L and was less sensitive to overdosing. TC was further examined for harvesting C. sorokiniana during FPWW treatment. The best performance (94 %) was achieved on day 15 at pH 5 using only 15 mg/L TC. Under these conditions, treated water met wastewater discharge standards for total nitrogen (8.5 mg/L) and total phosphorus (0.4 mg/L), and the biomass obtained high protein content (52.9 %), with minimal impact from TC on its quality. Techno-economic analysis showed that, while centrifugation (case study 2) yielded slightly higher biomass quality, the TC-based harvesting method with minimal centrifugation (case study 1) achieved a reduction of roughly 10 % in operating and annual capital costs. A sensitivity analysis indicated that labour cost, the cost of capital and the electricity price were the key cost drivers for both case studies in the base case scenario. Additionally, scale-up calculations with 10- and 100-fold increases in flow rate showed that case study 1 resulted in more moderate growth in operating and annual capital costs, showing a more economically sustainable option for large-scale microalgae recovery. • Tannin coagulant at 15 mg/L efficiently harvested C. sorokiniana from FPWW at pH 5. • Treated FPWW had TN (8.5 mg/L), TP (0.4 mg/L) and biomass contained 52.9 % protein. • TC-based harvesting had ∼10 % lower base case operating and annual capital costs. • Harvesting cost is driven by labour cost, cost of capital and electricity price. • TC-based harvesting showed lower cost escalation with scale-ups than centrifugation.

Chemical Engineering JournalVol. 524
Häme University of Applied Sciences (FI), University of Oulu (FI)
Openalex Percentile: Top 28%
Algal biology and biofuel production
0.73
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