FRINK Linked Data Fragments server

Matches in SemOpenAlex for { <https://semopenalex.org/work/W1567852815> ?p ?o ?g. }

• W1567852815 endingPage "527" @default.
• W1567852815 startingPage "509" @default.
• W1567852815 abstract "The combined removal of SO2 and CO2 using aqueous ammonia has many advantages over the conventional processes, such as the ability to capture multiple pollutants, the low cost of absorbent, high CO2 loading capacity, and the capacity to regenerate solvent at low temperature. In this paper, a closed-loop CO2 absorption-desorption process integrated with packed column flue gas desulfurization system was investigated. The CO2 absorption was modeled using the rigorous rate-based RateFrac model in Aspen Plus, whereas the SO2 column and CO2 stripper were modeled based on the RadFrac equilibrium model. The thermodynamic properties of the components were estimated with the Electrolyte NRTL model. The model was coupled with chemical equilibrium and kinetic reactions of the NH3-CO2-H2O and NH3-SO2-H2O system. The predicted results of temperature profile, variation in CO2 concentration along the column, SO2 removal efficiency, and CO2 separation rates agreed with published experimental results. To optimize the operating conditions, the impacts of performance parameters are investigated including flue gas temperature, concentration of CO2 and SO2 in flue gases, and the temperatures of the lean solution and ammoniated water. Furthermore, the performance efficiency of the stripper column is analyzed in terms of reboiler heat duty and CO2 regeneration rate, for the stripper operating pressure range of 2–20 bar and the stripper inlet temperature range of 60–105 °C. The results show that the suggested model is an adequate approach for the combined removal of CO2 and SO2 from the stack gases." @default.
• W1567852815 created "2016-06-24" @default.
• W1567852815 creator A5027604639 @default.
• W1567852815 creator A5043667413 @default.
• W1567852815 date "2014-04-21" @default.
• W1567852815 modified "2023-10-16" @default.
• W1567852815 title "Modeling and simulation of the combined removal of SO₂and CO₂by aqueous ammonia" @default.
• W1567852815 cites W1967373753 @default.
• W1567852815 cites W1968301827 @default.
• W1567852815 cites W1973403039 @default.
• W1567852815 cites W1976398354 @default.
• W1567852815 cites W1984376157 @default.
• W1567852815 cites W1984942265 @default.
• W1567852815 cites W1987424498 @default.
• W1567852815 cites W1994006590 @default.
• W1567852815 cites W1999714768 @default.
• W1567852815 cites W2003736021 @default.
• W1567852815 cites W2005567600 @default.
• W1567852815 cites W2008844191 @default.
• W1567852815 cites W2008933561 @default.
• W1567852815 cites W2009323309 @default.
• W1567852815 cites W2012794750 @default.
• W1567852815 cites W2013611472 @default.
• W1567852815 cites W2014119082 @default.
• W1567852815 cites W2015830500 @default.
• W1567852815 cites W2023063248 @default.
• W1567852815 cites W2023476868 @default.
• W1567852815 cites W2026016641 @default.
• W1567852815 cites W2026926751 @default.
• W1567852815 cites W2032188460 @default.
• W1567852815 cites W2032619003 @default.
• W1567852815 cites W2035292839 @default.
• W1567852815 cites W2042440827 @default.
• W1567852815 cites W2044401185 @default.
• W1567852815 cites W2053167154 @default.
• W1567852815 cites W2053310195 @default.
• W1567852815 cites W2054874170 @default.
• W1567852815 cites W2054902513 @default.
• W1567852815 cites W2059408291 @default.
• W1567852815 cites W2063271943 @default.
• W1567852815 cites W2063971768 @default.
• W1567852815 cites W2069277014 @default.
• W1567852815 cites W2072933626 @default.
• W1567852815 cites W2077083381 @default.
• W1567852815 cites W2079771206 @default.
• W1567852815 cites W2080695842 @default.
• W1567852815 cites W2080815644 @default.
• W1567852815 cites W2081238788 @default.
• W1567852815 cites W2081976482 @default.
• W1567852815 cites W2090337218 @default.
• W1567852815 cites W2099267719 @default.
• W1567852815 cites W2100417520 @default.
• W1567852815 cites W2102220872 @default.
• W1567852815 cites W2112393391 @default.
• W1567852815 cites W2115250949 @default.
• W1567852815 cites W2120012334 @default.
• W1567852815 cites W2129902060 @default.
• W1567852815 cites W2161240730 @default.
• W1567852815 cites W2256026001 @default.
• W1567852815 cites W2314454354 @default.
• W1567852815 cites W2317958734 @default.
• W1567852815 cites W2479700789 @default.
• W1567852815 cites W2806607778 @default.
• W1567852815 cites W3146843085 @default.
• W1567852815 cites W4234703063 @default.
• W1567852815 cites W4251981928 @default.
• W1567852815 doi "https://doi.org/10.1002/ghg.1420" @default.
• W1567852815 hasPublicationYear "2014" @default.
• W1567852815 type Work @default.
• W1567852815 sameAs 1567852815 @default.
• W1567852815 citedByCount "18" @default.
• W1567852815 countsByYear W15678528152014 @default.
• W1567852815 countsByYear W15678528152015 @default.
• W1567852815 countsByYear W15678528152016 @default.
• W1567852815 countsByYear W15678528152017 @default.
• W1567852815 countsByYear W15678528152018 @default.
• W1567852815 countsByYear W15678528152019 @default.
• W1567852815 countsByYear W15678528152020 @default.
• W1567852815 countsByYear W15678528152022 @default.
• W1567852815 countsByYear W15678528152023 @default.
• W1567852815 crossrefType "journal-article" @default.
• W1567852815 hasAuthorship W1567852815A5027604639 @default.
• W1567852815 hasAuthorship W1567852815A5043667413 @default.
• W1567852815 hasConcept C107706546 @default.
• W1567852815 hasConcept C121332964 @default.
• W1567852815 hasConcept C125287762 @default.
• W1567852815 hasConcept C131321042 @default.
• W1567852815 hasConcept C147789679 @default.
• W1567852815 hasConcept C150394285 @default.
• W1567852815 hasConcept C159985019 @default.
• W1567852815 hasConcept C162711632 @default.
• W1567852815 hasConcept C167206829 @default.
• W1567852815 hasConcept C178790620 @default.
• W1567852815 hasConcept C184651966 @default.
• W1567852815 hasConcept C185592680 @default.
• W1567852815 hasConcept C192562407 @default.
• W1567852815 hasConcept C2776382133 @default.
• W1567852815 hasConcept C68000547 @default.

• next