Viravid Na Nagara1, Zhiming Zhang1, Hadeer Saleh1, �Sameer Neve1, Rupali Datta2, Paul Truong3, Dibyendu Sarkar1
1 Department of Civil, Environmental, and Ocean Engineering, Stevens Institute of Technology, Hoboken, NJ, USA
2 Department of Biological Sciences, Michigan Technological University, Houghton, MI, USA
3 Veticon Consulting, Byron Bay, �New South Wales, Australia
Pollutant Removal Using Vetiver Grass and �Generation of Biofuel and Biochar From Spent Biomass: �A Circular Economy Model
Zhiming Zhang
(zzhan100@stevens.edu)
Hadeer Saleh
(hsaleh2@stevens.edu)
Sameer Neve
(sneve@stevens.edu)
Rupali Datta
(rupdatta@mtu.edu)
Paul Truong
(p.truong@veticon.com.au)
Dibyendu Sarkar
Viravid Na Nagara
Pollutant Removal Using Vetiver Grass and �Generation of Biofuel and Biochar From Spent Biomass: �A Circular Economy Model
Problems caused by stormwater runoff��
Source: https://twitter.com/jgodynick/status/1044673777341214722
https://patch.com/new-jersey/secaucus/dramatic-photos-secaucus-flooding-tuesday
Visible threat:
Invisible threat:
Problems caused by stormwater runoff��
Source: https://sigearth.com/stormwater-runoff-a-top-cause-of-water-pollution/
Metals
Nutrients
Total suspended solids
Problems caused by stormwater runoff��
Invisible threat: Stormwater pollution
Adverse environmental impacts
Source: https://www.draper.ut.us/1021/Pollution-Information�https://www.stevens.edu/news/how-stevens-helping-save-oceans-and-lakes-trimming-nutrient-runoff
Visible threat:
Invisible threat:
Vetiver (Chrysopogon zizanioides)
Parameter | Range of tolerance | |
pH | 3.3-12.5 | |
Temperature | Frost | 5°F (-15°C) |
Heat | 140°F (+60°C) | |
Drought | 15 months | |
Altitude | 2800 m | |
Source: http://vetiver.com.vn/vetiver-grass-system/
Floating treatment platform (FTP)
Objective
To develop a low-cost, efficient, “green” retrofit for stormwater retention ponds to enhance their metal and nutrient removal capacity and to use spent vetiver as feedstock for the generation of bioethanol and biochar to form a circular economy model.
Experimental design
Two �non-vegetated FTPs
(control)
Two �vegetated �FTPs
(vetiver)
30 mins
60 mins
90 mins
120 mins
1 �day
2 �days
3 days
6 �days
9�days
12 �days
15�days
18�days
21 days
24 days
28 days
Experimental design
1
2
3
4
5
Results – Pollutant Removal
NO3-
P
Results – Pollutant Removal
Cu
Pb
Zn
Results – Pollutant Removal
EDS spectrum of the sediment
keV
Results – Pollutant Distribution in Vetiver
Results – Plant growth and chlorophyll content
Results – Physicochemical characteristics of vetiver biochar
Parameter | Value |
Yield | 51.28% |
BET Surface Area | 171.6 m2/g |
pH | 9.78 ± 0.13 |
Electric Conductivity | 184.5 ± 21.3 µS/cm |
Ash Content | 23.6% |
Cation Exchange Capacity | 98 cmol/kg |
Bulk Density | 0.57 gm/ml |
C | 69.87 % |
H | 2.824 % |
O | 1.720 % |
N | 19.37 % |
H/C | 0.04 |
O/C | 0.025 |
N/C | 0.28 |
Liming Value | 3.06 % CaCO3 |
Biochar production:
The roots of the spent vetiver were washed clean, air dried, and ground before pyrolysis at 500℃ held for 60 mins.
Circular Economy
Results – Physicochemical characteristics of vetiver bioethanol
Parameter | Test method | Value |
Cellulose | Yang et al., 2006 | 32.86 % |
Hemicellulose | Yang et al., 2006 | 34.03 % |
Lignin | Yang et al., 2006 | 14.69 % |
Extractives | Yang et al., 2006 | 9.87 % |
Bioethanol Yield | Zabed et al., 2016 | 16.58 g/L �(236.89 mg/g) |
Ethanol Content | ASTM D 5501 | 98.86 % |
Density at 25°C | ASTM D 4052 | 0.77 g/mL |
Calorific Value | ASTM D 2014-96 | 31.36 MJ/kg |
Viscosity | ASTM D 88-94 | 1.02 cSt |
Sulfur content | ASTM D 3177-89 | 0.03 wt % |
Water content | ASTM D 95-70 | 1.01 % |
Research Octane Number | ASTM D 2699 | 107 |
Bioethanol production:
The bioethanol was generated from the shoots of the spent vetiver via multiple steps, including
1) preparation of biomass, �2) dilute acid-alkali pretreatment, �3) enzymatic hydrolysis, �4) bioethanol fermentation, and �5) distillation.
Yang, H., Yan, R., Chen, H., Zheng, C., Lee, D.H., Liang, D.T., 2006. In-depth investigation of biomass pyrolysis based on three major components: hemicellulose, cellulose and lignin. Energy & Fuels 20, 388–393.
Zabed, H., Sahu, J.N., Boyce, A.N., Faruq, G., 2016. Fuel ethanol production from lignocellulosic biomass: an overview on feedstocks and technological approaches. Renew. Sustain. energy Rev. 66, 751–774.
Results – Potential metal residues in biochar and bioethanol
Metal leaching potential from biochar:
a SPLP criterion: Higher of the health-based leachate criterion or aqueous practical quantitation levels (NJDEP, 2013)�b TCLP criterion: maximum concentrations of contaminants for the toxic characteristics from Title 40 CFR 261.24 - Toxicity characteristic�c NR: Not regulated
Metal contents in bioethanol:
USEPA, 1994. Method 1312: Synthetic precipitation leaching procedure
USEPA, 1992. Method 1311: Toxicity characteristic leaching procedure
NJDEP, 2013. Development of site-specific impact to ground water soil remediation standards using the synthetic precipitation leaching procedure.
Summary
Thank you !
Acknowledgement:
This work was supported by United States Environmental Protection Agency/New Jersey Department of Environmental Protection and National Oceanic and Atmospheric Administration/New Jersey Sea Grant Consortium.
We thank Paul Truong for presenting our research in ICV-7.