Tri‐Generation from Biomass and Residues; Options for the Co‐Production of Fischer‐Tropsch Liquids, Electricity, and Heat

Ouwens, C. Daey; Uil, H. den; Boenigter, H.

doi:10.1002/9780470694954.ch39

Cited by 2 publications

(2 citation statements)

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“…In this work, low-temperature FTS in a slurry phase reactor with conventional cobalt catalyst has been considered. This technology has been proven at commercial scale to achieve up to 80% CO conversion, , using syngas H 2 /CO ratio typically in the range 1.9–2, and to maximize the production of waxes, which is desirable for the production of high-quality diesel fuels . Co-based catalysts also exhibit high resistance to deactivation.…”

Section: Process Design and Modelingmentioning

confidence: 99%

Decentralized Production of Fischer–Tropsch Biocrude via Coprocessing of Woody Biomass and Wet Organic Waste in Entrained Flow Gasification: Techno-Economic Analysis

et al. 2017

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Section: Process Design and Modelingmentioning

confidence: 99%

Decentralized Production of Fischer–Tropsch Biocrude via Coprocessing of Woody Biomass and Wet Organic Waste in Entrained Flow Gasification: Techno-Economic Analysis

et al. 2017

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“…In terms of technology, a low-temperature FT synthesis (LTFT) in a slurry phase reactor with conventional cobalt catalyst has been chosen in this work. State-of-the-art LTFT synthesis using CO-based catalysts has been proven on a commercial scale to achieve up to 80% CO conversion , and to maximize the production of waxes, which is desirable for the production of high-quality diesel fuels . CO-based catalysts have also been shown to exhibit high resistance to deactivation.…”

Section: Process Analysismentioning

confidence: 99%

CHP-Integrated Fischer-Tropsch Biocrude Production under Norwegian Conditions: Techno-Economic Analysis

et al. 2015

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This article presents a detailed techno-economic analysis, under Norwegian conditions, for the production of biocrude from woody biomass via high temperature entrained flow gasification and Fischer−Tropsch (FT) synthesis with integrated coproduction of heat and electricity. Biomass pretreatment based on both conventional drying and torrefaction processes are considered as options. Maximum calculated efficiency of biocrude at lower and upper bound CO conversions of 40% and 80% at the gasifier operating conditions of lambda value 0.2 and temperature 1300°C are 27% and 44%, respectively. Under these conditions, maximum thermal and net electrical efficiency are 55% and 15.5%, respectively. The economic viability of the biocrude production for plant capacities in the range of 150−600 MW thermal input has been evaluated as a function of the type of biomass pretreatment, gasification operating conditions, and the heat to electricity production ratios. Results from the economic analysis show that coproduction of biocrude combined with 100% heat production for district heating gives the lowest biocrude cost under Norwegian conditions, with large variations as the electricity to heat production ratio increases.

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Tri‐Generation from Biomass and Residues; Options for the Co‐Production of Fischer‐Tropsch Liquids, Electricity, and Heat

Cited by 2 publications

References 1 publication

Decentralized Production of Fischer–Tropsch Biocrude via Coprocessing of Woody Biomass and Wet Organic Waste in Entrained Flow Gasification: Techno-Economic Analysis

Decentralized Production of Fischer–Tropsch Biocrude via Coprocessing of Woody Biomass and Wet Organic Waste in Entrained Flow Gasification: Techno-Economic Analysis

CHP-Integrated Fischer-Tropsch Biocrude Production under Norwegian Conditions: Techno-Economic Analysis

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