FRINK Linked Data Fragments server

Matches in SemOpenAlex for { <https://semopenalex.org/work/W2073995003> ?p ?o ?g. }

• W2073995003 abstract "Abstract During LNG liquefaction, CO2 component in natural gas has to be removedcompletely to prevent icing and plugging in the system. The CO2 removal systemmay be the most important part in gas treatment system. Acceptable CO2 level oftypical 50 ppm in feed gas is very stringent and hard to meet. H2O in feed gasis relatively easily removed by molecular sieve type dehydration system. However, CO2 removal system requires complicated amine contactor andregeneration system with substantial heat source. Especially in floatingenvironment operation, reducing CO2 level could be the most critical part ofthe FLNG availability, consequently, continuation of LNG liquefaction operationin severe weather condition may be determined by the CO2 removal capability, whereas the cryogenic liquefaction part may affect production performance only.DSME has developed highly efficient and CO2 tolerant LNG liquefaction systemcalled Cluster LNG with increased pressure liquefaction and associatedcontainment system. The developed system accepts approximately 1% of CO2 forthe liquefaction and related systems. The CO2 tolerant characteristics of theliquefaction process will provide multifold safety margin against CO2 problemsin cryogenic systems and valves. Moreover, when CO2 level is less than 1%, theCO2 removal system may be eliminated from the liquefaction plant. Extensiveverification tests of different CO2 contents in the developed process have beencarried out, and found that experimental results are well coincident withtheoretical expectations. In addition, CO2 removal system and related testshave been carried out. From the experiment, possibility of CO2 removal system(CO2 2 ~ 5%) other than traditional amine base system has been investigated andnew concept CO2 removal system is being developed. The non-conventional CO2removal system, which includes icing and solid removal with hydro-cyclone, isbeing tested in a bench scale pilot plant. The new CO2 removal system combinedwith increased pressure liquefaction process will bring competitiveness innatural gas liquefaction. The developed system may accelerate monetization ofstranded gas fields with low unit liquefaction and gas treatment cost. 1. Backgrounds Lowering final delivery price to end-users would be important for businesssurvival in energy industry. To cope with the fundamental task, finding moreeconomic ways to transport gas from production sites to consumers have beenendeavored for many years. Among them, LNG is one of the efficient methods forlong distance and large volume gas transportation. But for the production ofLNG, stringent gas treatment, highly expensive liquefaction, transportation, and regasification systems have to be adequately prepared, which ultimatelyaffects the final gas delivery cost. In order to produce LNG, CO2 level in feed gas has to be removed, typicallyless than 50 ppm, to prevent ice formation during liquefaction. However, theCO2 removal to such low level is necessary only for liquefaction interimpurpose considered that most of the gas consumers such as gas engines andboilers tolerate certain percentages of CO2, at least up to pipeline gasquality, in the feed gas. With the reason, if CO2 tolerant LNG productionsystem is developed, it would be equally acceptable." @default.
• W2073995003 created "2016-06-24" @default.
• W2073995003 creator A5053296598 @default.
• W2073995003 creator A5079700164 @default.
• W2073995003 creator A5087234700 @default.
• W2073995003 date "2012-04-30" @default.
• W2073995003 modified "2023-10-16" @default.
• W2073995003 title "Development of CO2 Tolerant LNG Production System" @default.
• W2073995003 doi "https://doi.org/10.4043/23261-ms" @default.
• W2073995003 hasPublicationYear "2012" @default.
• W2073995003 type Work @default.
• W2073995003 sameAs 2073995003 @default.
• W2073995003 citedByCount "3" @default.
• W2073995003 countsByYear W20739950032013 @default.
• W2073995003 countsByYear W20739950032014 @default.
• W2073995003 countsByYear W20739950032022 @default.
• W2073995003 crossrefType "proceedings-article" @default.
• W2073995003 hasAuthorship W2073995003A5053296598 @default.
• W2073995003 hasAuthorship W2073995003A5079700164 @default.
• W2073995003 hasAuthorship W2073995003A5087234700 @default.
• W2073995003 hasConcept C127413603 @default.
• W2073995003 hasConcept C14034172 @default.
• W2073995003 hasConcept C187320778 @default.
• W2073995003 hasConcept C191859794 @default.
• W2073995003 hasConcept C21880701 @default.
• W2073995003 hasConcept C39432304 @default.
• W2073995003 hasConcept C548081761 @default.
• W2073995003 hasConcept C59427239 @default.
• W2073995003 hasConcept C69907114 @default.
• W2073995003 hasConcept C78519656 @default.
• W2073995003 hasConceptScore W2073995003C127413603 @default.
• W2073995003 hasConceptScore W2073995003C14034172 @default.
• W2073995003 hasConceptScore W2073995003C187320778 @default.
• W2073995003 hasConceptScore W2073995003C191859794 @default.
• W2073995003 hasConceptScore W2073995003C21880701 @default.
• W2073995003 hasConceptScore W2073995003C39432304 @default.
• W2073995003 hasConceptScore W2073995003C548081761 @default.
• W2073995003 hasConceptScore W2073995003C59427239 @default.
• W2073995003 hasConceptScore W2073995003C69907114 @default.
• W2073995003 hasConceptScore W2073995003C78519656 @default.
• W2073995003 hasLocation W20739950031 @default.
• W2073995003 hasOpenAccess W2073995003 @default.
• W2073995003 hasPrimaryLocation W20739950031 @default.
• W2073995003 hasRelatedWork W144558470 @default.
• W2073995003 hasRelatedWork W177975684 @default.
• W2073995003 hasRelatedWork W1807437098 @default.
• W2073995003 hasRelatedWork W1991361785 @default.
• W2073995003 hasRelatedWork W2144318898 @default.
• W2073995003 hasRelatedWork W2192264510 @default.
• W2073995003 hasRelatedWork W2361699404 @default.
• W2073995003 hasRelatedWork W2784092087 @default.
• W2073995003 hasRelatedWork W3211853770 @default.
• W2073995003 hasRelatedWork W2188695353 @default.
• W2073995003 isParatext "false" @default.
• W2073995003 isRetracted "false" @default.
• W2073995003 magId "2073995003" @default.
• W2073995003 workType "article" @default.