FRINK Linked Data Fragments server

Matches in SemOpenAlex for { <https://semopenalex.org/work/W2316841259> ?p ?o ?g. }

• W2316841259 abstract "It is important to evaluate the solubility of solid carbon dioxide in liquefied natural gas for natural gas liquefaction at relatively high temperature. The regular solution method and the equations-of-state (EOS) are used to calculate the solubility of carbon dioxide in saturated liquid methane in this paper. The calculation results are compared with the experiment data, and it certifies that the EOS method can be recommended for this kind of solubility calculation. In addition, nitrogen and ethane are common components in natural gas. In this paper, PR EOS is selected to calculate the solubility of carbon dioxide in CH4+N2 and CH4+C2H6 mixtures. Results show that the solubility of carbon dioxide in liquid CH4+N2 mixtures increases with the addition of nitrogen content in the relatively low temperature region (lower than 155K). With the temperature increases, the solubility of carbon dioxide decreases with the increase of nitrogen content. While in liquid CH4+C2H6 mixtures, it increases with the increase of ethane content. liquid nitrogen, liquid oxygen or LNG. In 1940, Fedorova calculated the solubility of carbon dioxide in liquid oxygen and in liquid nitrogen according to ideal solution theory. At the same time, he did some experiments and found that the theoretical calculations are more than 100 times larger than the experimental values(7). In 1962, Davis et al performed a series of experiments on the methane-carbon dioxide system and got the solubility of carbon dioxide in methane at different temperatures(8). Most of these researchers are experts in the field of chemistry, who were focus on a variety of experimental methods of solubility determination. Li from Zhejiang University used the regular solution method and modified Scatchard-Hildebrand relation in her PhD thesis to calculate the solubility of carbon dioxide in liquid nitrogen and liquid oxygen, and obtained good results(9). As liquid methane is a cryogenic non-polar liquid similar with liquid nitrogen and liquid oxygen, similar method has been imitated in the calculation of the solubility of carbon dioxide in the saturated liquid methane in this paper. Additionally, simple cubic equations-of-state has been widely used in non-polar fluid phase equilibria calculations. In 2006, ZareNezhad and Eggeman(10) used PR EOS to predict CO2 freezing points of hydrocarbon liquid and vapor mixtures at cryogenic conditions of gas plants. The overall average absolute relative deviation between the experimental and predicted CO2 freezing temperatures for this binary system is 0.26%. So EOS method is selected for the solid-liquid phase equilibria calculation in this paper." @default.
• W2316841259 created "2016-06-24" @default.
• W2316841259 creator A5051594417 @default.
• W2316841259 creator A5077775027 @default.
• W2316841259 date "2011-01-01" @default.
• W2316841259 modified "2023-09-27" @default.
• W2316841259 title "Calculation of Carbon Dioxide Solubility in Liquefied Natural Gas" @default.
• W2316841259 cites W1514777804 @default.
• W2316841259 cites W1526438118 @default.
• W2316841259 cites W2013462209 @default.
• W2316841259 cites W2027190349 @default.
• W2316841259 cites W2057662344 @default.
• W2316841259 cites W2065713301 @default.
• W2316841259 cites W2103198964 @default.
• W2316841259 cites W2129288307 @default.
• W2316841259 cites W2131201603 @default.
• W2316841259 cites W2154161858 @default.
• W2316841259 cites W2376008039 @default.
• W2316841259 cites W2581933137 @default.
• W2316841259 cites W2731138126 @default.
• W2316841259 cites W3041714850 @default.
• W2316841259 doi "https://doi.org/10.7763/ijcea.2011.v2.135" @default.
• W2316841259 hasPublicationYear "2011" @default.
• W2316841259 type Work @default.
• W2316841259 sameAs 2316841259 @default.
• W2316841259 citedByCount "0" @default.
• W2316841259 crossrefType "journal-article" @default.
• W2316841259 hasAuthorship W2316841259A5051594417 @default.
• W2316841259 hasAuthorship W2316841259A5077775027 @default.
• W2316841259 hasConcept C104779481 @default.
• W2316841259 hasConcept C130622031 @default.
• W2316841259 hasConcept C140205800 @default.
• W2316841259 hasConcept C155574463 @default.
• W2316841259 hasConcept C159985019 @default.
• W2316841259 hasConcept C161790260 @default.
• W2316841259 hasConcept C178790620 @default.
• W2316841259 hasConcept C179104552 @default.
• W2316841259 hasConcept C185592680 @default.
• W2316841259 hasConcept C191859794 @default.
• W2316841259 hasConcept C192562407 @default.
• W2316841259 hasConcept C22884784 @default.
• W2316841259 hasConcept C24596552 @default.
• W2316841259 hasConcept C512735826 @default.
• W2316841259 hasConcept C516920438 @default.
• W2316841259 hasConcept C530467964 @default.
• W2316841259 hasConcept C537208039 @default.
• W2316841259 hasConceptScore W2316841259C104779481 @default.
• W2316841259 hasConceptScore W2316841259C130622031 @default.
• W2316841259 hasConceptScore W2316841259C140205800 @default.
• W2316841259 hasConceptScore W2316841259C155574463 @default.
• W2316841259 hasConceptScore W2316841259C159985019 @default.
• W2316841259 hasConceptScore W2316841259C161790260 @default.
• W2316841259 hasConceptScore W2316841259C178790620 @default.
• W2316841259 hasConceptScore W2316841259C179104552 @default.
• W2316841259 hasConceptScore W2316841259C185592680 @default.
• W2316841259 hasConceptScore W2316841259C191859794 @default.
• W2316841259 hasConceptScore W2316841259C192562407 @default.
• W2316841259 hasConceptScore W2316841259C22884784 @default.
• W2316841259 hasConceptScore W2316841259C24596552 @default.
• W2316841259 hasConceptScore W2316841259C512735826 @default.
• W2316841259 hasConceptScore W2316841259C516920438 @default.
• W2316841259 hasConceptScore W2316841259C530467964 @default.
• W2316841259 hasConceptScore W2316841259C537208039 @default.
• W2316841259 hasLocation W23168412591 @default.
• W2316841259 hasOpenAccess W2316841259 @default.
• W2316841259 hasPrimaryLocation W23168412591 @default.
• W2316841259 hasRelatedWork W1986604600 @default.
• W2316841259 hasRelatedWork W2004924501 @default.
• W2316841259 hasRelatedWork W2006098505 @default.
• W2316841259 hasRelatedWork W2012847848 @default.
• W2316841259 hasRelatedWork W2019388642 @default.
• W2316841259 hasRelatedWork W2023034902 @default.
• W2316841259 hasRelatedWork W2026800747 @default.
• W2316841259 hasRelatedWork W2078275594 @default.
• W2316841259 hasRelatedWork W2093611123 @default.
• W2316841259 hasRelatedWork W2133184274 @default.
• W2316841259 hasRelatedWork W2135729873 @default.
• W2316841259 hasRelatedWork W2158974466 @default.
• W2316841259 hasRelatedWork W2384854067 @default.
• W2316841259 hasRelatedWork W2563344409 @default.
• W2316841259 hasRelatedWork W2791382040 @default.
• W2316841259 hasRelatedWork W2976158042 @default.
• W2316841259 hasRelatedWork W37389710 @default.
• W2316841259 hasRelatedWork W792674225 @default.
• W2316841259 hasRelatedWork W814891430 @default.
• W2316841259 hasRelatedWork W851838231 @default.
• W2316841259 isParatext "false" @default.
• W2316841259 isRetracted "false" @default.
• W2316841259 magId "2316841259" @default.
• W2316841259 workType "article" @default.