FRINK Linked Data Fragments server

Matches in SemOpenAlex for { <https://semopenalex.org/work/W2945787179> ?p ?o ?g. }

• W2945787179 endingPage "1079" @default.
• W2945787179 startingPage "1071" @default.
• W2945787179 abstract "Renewables are steadily growing becoming a significant part of the global energy mix, in particular in the power sector. An attractive solution could be represented by Power to Gas (PtG), an energy storage strategy. In the PtG process renewable or excess electric energy is used for water electrolysis to produce hydrogen that is then combined with CO2 and converted into methane (synthetic or substitute natural gas, SNG) through the Sabatier reaction. SNG is particularly interesting because leads to an easily transportable (in the existing infrastructures) fuel with a wide proven market for power, thermal and mobility final use applications. The key issue consist on putting together green hydrogen produced by electrolysis fed by renewables with high content CO2 gases supplied from different sources (e.g. syngas from gasification, biogas, geothermic fields, soil gas and gas wells). In this work the CO2 hydrogenation process, coupled with renewables, has been study in a modular, moveable, skidable plant, in the scale of 0.2–1 Nm3/h of produced SNG. The pilot plant is equipped with a methanation unit constituted by a multi-tubular fixed bed reactor able to work in cooled or adiabatic conditions; water produced is separated by a plate&shell condenser. Several sensors, an online gas analysis system and a data acquisition system allow monitoring continuous experimental tests. The methanation facility is able to work in the range of 1–5 bars. The paper reports the results of first experimental activities related to SNG production with Ru based supported catalyst. The experimental activity was carried out in order to check the operability of all components and to improve the knowledge on methanation process in different conditions relevant to Power-to-Gas applications. Different weighted hourly space velocity (WHSV), gas inlet composition, reagent mixture, H2/CO2 ratio, temperature and pressure conditions have been investigated. Increasing pressure drives CH4 production as CO2 conversion is kinetically boosted by raising pressure. Results show that a decreasing trend of XCO2 is observed by increasing WHSV. Results indicate high CO2 per pass conversion with CO2/H2 concentrate feed using Ru based catalyst. Finally the effect of CH4 in the feed was studied emulating two reactors in series. Biogas representative CO2/H2/CH4 mixtures were tested in order to study direct methanation as a biogas upgrading technology." @default.
• W2945787179 created "2019-05-29" @default.
• W2945787179 creator A5050951509 @default.
• W2945787179 creator A5061537667 @default.
• W2945787179 creator A5081820577 @default.
• W2945787179 creator A5086542315 @default.
• W2945787179 date "2019-10-01" @default.
• W2945787179 modified "2023-10-06" @default.
• W2945787179 title "P2G movable modular plant operation on synthetic methane production from CO2 and hydrogen from renewables sources" @default.
• W2945787179 cites W1940496428 @default.
• W2945787179 cites W1981891771 @default.
• W2945787179 cites W1982189046 @default.
• W2945787179 cites W2014043158 @default.
• W2945787179 cites W2057457710 @default.
• W2945787179 cites W2066558407 @default.
• W2945787179 cites W2074161927 @default.
• W2945787179 cites W2075228459 @default.
• W2945787179 cites W2090633687 @default.
• W2945787179 cites W2113570021 @default.
• W2945787179 cites W2164124764 @default.
• W2945787179 cites W2186567173 @default.
• W2945787179 cites W2234140931 @default.
• W2945787179 cites W2283110264 @default.
• W2945787179 cites W2555143474 @default.
• W2945787179 cites W2592550262 @default.
• W2945787179 cites W2616638000 @default.
• W2945787179 cites W2620912375 @default.
• W2945787179 cites W2736740475 @default.
• W2945787179 cites W2744259153 @default.
• W2945787179 cites W2753273584 @default.
• W2945787179 cites W2753843468 @default.
• W2945787179 cites W2754466543 @default.
• W2945787179 cites W2769215390 @default.
• W2945787179 cites W2775406497 @default.
• W2945787179 cites W2791935119 @default.
• W2945787179 cites W2794392169 @default.
• W2945787179 cites W2796317787 @default.
• W2945787179 cites W4234390125 @default.
• W2945787179 doi "https://doi.org/10.1016/j.fuel.2019.05.074" @default.
• W2945787179 hasPublicationYear "2019" @default.
• W2945787179 type Work @default.
• W2945787179 sameAs 2945787179 @default.
• W2945787179 citedByCount "52" @default.
• W2945787179 countsByYear W29457871792020 @default.
• W2945787179 countsByYear W29457871792021 @default.
• W2945787179 countsByYear W29457871792022 @default.
• W2945787179 countsByYear W29457871792023 @default.
• W2945787179 crossrefType "journal-article" @default.
• W2945787179 hasAuthorship W2945787179A5050951509 @default.
• W2945787179 hasAuthorship W2945787179A5061537667 @default.
• W2945787179 hasAuthorship W2945787179A5081820577 @default.
• W2945787179 hasAuthorship W2945787179A5086542315 @default.
• W2945787179 hasBestOaLocation W29457871792 @default.
• W2945787179 hasConcept C105923489 @default.
• W2945787179 hasConcept C115626544 @default.
• W2945787179 hasConcept C119599485 @default.
• W2945787179 hasConcept C123703457 @default.
• W2945787179 hasConcept C127413603 @default.
• W2945787179 hasConcept C14518398 @default.
• W2945787179 hasConcept C147789679 @default.
• W2945787179 hasConcept C161790260 @default.
• W2945787179 hasConcept C163127949 @default.
• W2945787179 hasConcept C174575960 @default.
• W2945787179 hasConcept C17525397 @default.
• W2945787179 hasConcept C178790620 @default.
• W2945787179 hasConcept C185592680 @default.
• W2945787179 hasConcept C188573790 @default.
• W2945787179 hasConcept C194439259 @default.
• W2945787179 hasConcept C202189072 @default.
• W2945787179 hasConcept C202417442 @default.
• W2945787179 hasConcept C21880701 @default.
• W2945787179 hasConcept C26625249 @default.
• W2945787179 hasConcept C39432304 @default.
• W2945787179 hasConcept C512968161 @default.
• W2945787179 hasConcept C516920438 @default.
• W2945787179 hasConcept C548081761 @default.
• W2945787179 hasConcept C55493867 @default.
• W2945787179 hasConcept C59427239 @default.
• W2945787179 hasConcept C68801617 @default.
• W2945787179 hasConcept C7453809 @default.
• W2945787179 hasConcept C75212476 @default.
• W2945787179 hasConceptScore W2945787179C105923489 @default.
• W2945787179 hasConceptScore W2945787179C115626544 @default.
• W2945787179 hasConceptScore W2945787179C119599485 @default.
• W2945787179 hasConceptScore W2945787179C123703457 @default.
• W2945787179 hasConceptScore W2945787179C127413603 @default.
• W2945787179 hasConceptScore W2945787179C14518398 @default.
• W2945787179 hasConceptScore W2945787179C147789679 @default.
• W2945787179 hasConceptScore W2945787179C161790260 @default.
• W2945787179 hasConceptScore W2945787179C163127949 @default.
• W2945787179 hasConceptScore W2945787179C174575960 @default.
• W2945787179 hasConceptScore W2945787179C17525397 @default.
• W2945787179 hasConceptScore W2945787179C178790620 @default.
• W2945787179 hasConceptScore W2945787179C185592680 @default.
• W2945787179 hasConceptScore W2945787179C188573790 @default.
• W2945787179 hasConceptScore W2945787179C194439259 @default.
• W2945787179 hasConceptScore W2945787179C202189072 @default.
• W2945787179 hasConceptScore W2945787179C202417442 @default.

• next