Techno‐Economic Evaluation of Photocatalytic H2S Splitting. Issue 8 (3rd June 2021)

• Record Type: Journal Article
• Authors: Oladipo, Habeebllah; Yusuf, Ahmed; Al-Ali, Khalid; Palmisano, Giovanni
• Is Part Of: Energy technology. Volume 9:Issue 8(2021)
• Page Start: n/a
• Page End: n/a
• Publication Date: 2021-06-03
• Subjects: ASPEN Plus -- H2S splitting -- hydrogen -- photocatalysis -- techno-economic assessments; Energy development -- Periodicals; Power resources -- Periodicals; 333.79
• DOI: 10.1002/ente.202100163
• Languages: English
• ISSNs: 2194-4288

Abstract

Abstract : The removal of the noxious H2 S from natural gas remains a challenging task in the oil and gas industry. Different H2 S splitting technologies are proposed and investigated based on the techno‐economic analysis. Herein, the photocatalysis route for H2 S splitting represents a potential technology that is not yet fully analyzed. The present study reports a techno‐economic analysis of hydrogen production from H2 S via photocatalysis. Guided by the previous experimental result on H2 S splitting, Aspen Plus software is used to design and simulate the proposed plant. An economic analysis is performed with CapCost software to estimate the plant capital expenditure (CAPEX) and operational expenditure (OPEX) and the cost of hydrogen production. At 0.485 t H2 per h, the process CAPEX is about 105 M$, and OPEX is 143 M$ per year. At a levelized cost of hydrogen (LCOH) production of 1860 $ per t H2, the proposed plant will be able to break even at the end of the plant life. Sensitivity analysis reveals that the process OPEX and price of hydrogen are strongly dependent on the cost of aqueous NaOH. These findings are potentially useful for oil and gas industries looking to incorporate an emerging technology like the presented one in refineries. Abstract : This study presents a techno‐economic assessment of photocatalytic hydrogen production from H2 S and aqueous NaOH solution in a slurry batch reactor. Hydrogen production is simulated using ASPEN plus V8.4 process simulator, and economic calculation is performed using CAPCOST. This process is a potentially sustainable alternative for sour gas sweetening in natural gas processing.