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dc.contributor.authorTrasti, Eivind Johan Rokstad
dc.contributor.authorNumme, Oliver
dc.contributor.authorLarsen, Sebastian
dc.date.accessioned2024-03-11T08:39:07Z
dc.date.available2024-03-11T08:39:07Z
dc.date.issued2023
dc.identifier.urihttps://hdl.handle.net/11250/3121693
dc.description.abstractDimethyl ether (DME) and other synthetic fuels are essential for the transition to a fossil-free transport sector. DME brings with it several advantages in today´s infrastructure and is well comparable with diesel in existing combustion engines. It will require 1.74 times as much liter DME to drive the same distance as with diesel. However, a mixture of DME and diesel will reduce greenhouse gas emissions and range. DME can be produced from synthesis gas via gasification of carbonneutral resources such as biomass and is then a green alternative. The synthesis gas can be used to produce DME directly in a one-step process (direct conversion), or via methanol in a two-step process (indirect conversion). In this bachelor´s thesis, the process simulations in Aspen Hysys DME synthesis from methanol have been studied. The task in the study involved assessment of process design, process- and energy optimization, as well as cost estimation of DME synthesis. It started with a sensitivity analysis that contained evaluation of operating parameters such as pressure and temperature, as well as reactor design. Furthermore, the thermodynamic models (PRSV, NRTL, UNIQUAC and Wilson) in Aspen Hysys were simulated and compared. Then energy optimization of the process was carried out with internal heat integration and external heat transfer in the form of cooling water and steam. Finally, cost estimation of "base case", parameter and energy optimization were carried out. Before the profitability analysis, the project had a capital expenditure (CAPEX) of 1.8 million USD, operating expenses (OPEX) of 58.6 million USD and revenue of 54.3 million USD. However, profitability and operating expenses depend on the price of DME and methanol. The results from the optimization gave higher DME flow (0.5 %), lower energy demand (-46 %), lower OPEX (-11 %) and CAPEX (-4 %), as well as higher income (0.5 %) compared to "base case".en_US
dc.language.isonoben_US
dc.publisherUniversity of South-Eastern Norwayen_US
dc.subjectbiomassen_US
dc.subjectgasificationen_US
dc.subjectsynthesis gasen_US
dc.subjectmethanolen_US
dc.subjectdimethyl etheren_US
dc.subjectaspen hysysen_US
dc.titleGrønn produksjon av dimetyleter (DME) – Indirekte konvertering av syntesegass fra biomasseen_US
dc.typeBachelor thesisen_US
dc.description.versionpublishedVersionen_US
dc.rights.holderCopyright The Author(s)en_US


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