AP2

Dr Aditya Putranto


Senior Lecturer in Chemical Engineering
PhD SFHEA

About

Areas of specialism

sustainability systems; sustainability assessment; decision-making tools for sustainability interventions; life-cycle environment analysis; techno-economic analysis; circular economy ; process modeling and simulation; sustainable energy; sustainable environment; sustainable food

My qualifications

PhD
Monash University Australia
MSc
UNSW
MEng
Bandung Institute of Technology
BEng
Bandung Institute of Technology

Affiliations and memberships

Advance Higher Education Academy
Senior Fellow Higher Education Academy (SFHEA) UK
PR275895

Research

Research interests

Teaching

Publications

Highlights

 

Full publications are accessible in Google Scholar https://scholar.google.co.uk/citations?user=zocjfgEAAAAJ&hl=en

 

Selected publications:

Ng, Z.W., Yeoh, K.Y., Hafyan, R.H., Putranto, A., Horri, B.A., Zein, S.H., Rhamdhani, M.A., Aziz, M., Butar, I., 2024. Technoeconomic analysis of production of octane booster components derived from lignin. Biomass Conversion and Biorefineryhttps://doi.org/10.1007/s13399-023-05255-w

Santoso, E.E., Saptoro, A., Kumar, P., Tiong, A.N.T., Putranto, A., Suherman, S., 2023. 7E+Q analysis: a new multidimensional assessment tools for solar drying of food and agricultural products. Environment, Development and Sustainabilityhttps://doi.org/10.1007/s10668-023-03341-7

Mohammed, M.Z.R., Ng, Z.W., Putranto, A., Kong, Z.Y., Sunarso, J. Aziz, A., Hein, S.H., Giwangkara, J., Butar, I. 2023. Process design, simulation and techno-economic analysis of integrated production of furfural and glucose derived from palm oil empty bunch. Clean Technology and Environment Protection (2023). https://doi.org/10.1007/s10098-022-02454-3

Ng, Z.W., Gan, H.X., Putranto, A., Rhamdhani, M.A., Zein, S.H., George, O.A. Giwangara, J., Butar, I., 2022. Process design and life cyc­­­le assessment of furfural and glucose co-production derived from palm oil empty fruit bunches. Environment, Development and Sustainability https://doi.org/10.1007/s10668-022-02633-8

Zein, S.H., Grogan, C.T., Yansaneh, O.Y., Putranto, A., 2022. Pyrolysis of high density polyethylene waste plastic to liquid fuels – Modeling and economic analysis. Processes 10 (8), 1503. 

Putranto, A., Hadibarata, T., Aziz, M., Yeo, J.Y.Y., Ismadji, S., Sunarso, J. 2022., Effects of pyrolysis temperature and impregnation ratio on adsorption kinetics and isotherm of methylene blue on corn cobs activated carbons. South African Journal in Chemical Engineering 42, 91-97.

Aziz, M., Putranto, A., Biddinika, M.K., Wijayanto, A.T., 2017. Energy saving combination of N2 production, NH3 synthesis and power generation. International Journal of Hydrogen Energy 42, 27174-27183

Bahman Amini Horri, Zi Wei Ng, King Yee Yeoh, Rendra Hakim Hafyan, Aditya Putranto, Bahman Amini Horri, Sharif H. Zein, Makbar Rhamdhani, Muhammad Aziz, Ivan Butar (2024)Techno-economic analysis of production of octane booster components derived from lignin, In: Biomass Conversion and Biorefinery Springer

In this study, a comprehensive process for production of an environmentally friendly octane booster (acetophenone) from lignin is presented, along with a detailed techno-economic analysis. Recognizing that much of the prior research on octane boosters has been confined to experimental lab-level investigations, this study develops comprehensive process design to unravel the intricacies of large-scale acetophenone production. The acetophenone production process involves catalytic hydrogenolysis, which also yields phenol as a valuable side product. Based on the process flow diagram, mass and energy balances were developed, revealing significantly improved yields and purity of acetophenone compared to industry standards, reaching 0.74 kg acetophenone per kg of lignin and 99 wt%. In the techno-economic analysis, calculations involving fixed capital investment (FCI), operating costs, and working capital were conducted based on a feed of 100 kg/h of dry lignin. The results indicate FCI at 2.72 million USD, operating costs at 1.09 million USD per year, and working capital at 0.57 million USD. Assuming a 20-year operational lifespan, the payback period is estimated at 6.09 years, as depicted by the cumulative cash flow diagram. Moreover, techno-economic analysis demonstrates a net present value (NPV) of 3.24 million USD at a 10% discount rate, an internal rate of return (IRR) of 22.73%, and a return on investment (ROI) of 34.39%. These positive outcomes underscore the robust profitability of the proposed acetophenone production plant derived from lignin. Additionally, a sensitivity analysis on the IRR indicates that increasing the production capacity could further enhance profitability, reaffirming the feasibility of the plant's operation. Crucially, this study highlights the potential for sustainable and economically viable production of acetophenone, offering an environmentally friendly alternative to toxic octane boosters and advancing the development of sustainable fuel additives.