Matches in SemOpenAlex for { <https://semopenalex.org/work/W2896434232> ?p ?o ?g. }
Showing items 1 to 97 of
97
with 100 items per page.
- W2896434232 endingPage "963" @default.
- W2896434232 startingPage "955" @default.
- W2896434232 abstract "Abstract BACKGROUND To date, none of the existing techno‐economic analyses on natural gas dehydration via absorption using triethylene glycol takes into consideration the profit assessment. This work addresses this shortcoming by developing a techno‐economic framework that evaluates the economic feasibility of three different dehydration processes, i.e., conventional dehydration process, stripping gas dehydration process using sale gas, and stripping gas dehydration process using nitrogen, which can meet the maximum water dew point requirement set by local authorities (e.g., Malaysia) for pipeline‐transported natural gas. RESULTS Our techno‐economic analyses reveal that the maximum water dew point specification of −25 °C can only be achieved by using a stripping gas dehydration process that consumes more than 260 Nm 3 h −1 of sale gas or 435 Nm 3 h −1 of nitrogen. In particular, the use of sale gas as stripping gas with an optimum flow rate of 260 Nm 3 h −1 generates the highest annual net profit margin, of about $29 million. Such a profit margin is higher with respect to the use of nitrogen as stripping gas and the conventional dehydration process by about $1.6 million and $300 000, respectively. The minimum water dew point specification of 5 °C, on the other hand, can be achieved by all three analysed dehydration processes. CONCLUSION The use of sale gas as stripping gas becomes more justifiable economically relative to the conventional dehydration process and the other alternative (the use of nitrogen as stripping gas) and when a low water dew point specification of −25 °C is required for natural gas. © 2018 Society of Chemical Industry" @default.
- W2896434232 created "2018-10-26" @default.
- W2896434232 creator A5004917138 @default.
- W2896434232 creator A5019010033 @default.
- W2896434232 creator A5019020773 @default.
- W2896434232 creator A5034037577 @default.
- W2896434232 date "2018-12-04" @default.
- W2896434232 modified "2023-09-27" @default.
- W2896434232 title "Development of a techno-economic framework for natural gas dehydration via absorption using Tri-Ethylene Glycol: a comparative study on conventional and stripping gas dehydration processes" @default.
- W2896434232 cites W1970295957 @default.
- W2896434232 cites W1974378163 @default.
- W2896434232 cites W1976276853 @default.
- W2896434232 cites W2005025925 @default.
- W2896434232 cites W2029308613 @default.
- W2896434232 cites W2055367582 @default.
- W2896434232 cites W2056849123 @default.
- W2896434232 cites W2084441490 @default.
- W2896434232 cites W2234466392 @default.
- W2896434232 cites W2481042602 @default.
- W2896434232 cites W2501767533 @default.
- W2896434232 cites W2502919292 @default.
- W2896434232 cites W2531385348 @default.
- W2896434232 cites W2558659911 @default.
- W2896434232 cites W2807701938 @default.
- W2896434232 cites W2884424602 @default.
- W2896434232 cites W2942557061 @default.
- W2896434232 doi "https://doi.org/10.1002/jctb.5844" @default.
- W2896434232 hasPublicationYear "2018" @default.
- W2896434232 type Work @default.
- W2896434232 sameAs 2896434232 @default.
- W2896434232 citedByCount "13" @default.
- W2896434232 countsByYear W28964342322019 @default.
- W2896434232 countsByYear W28964342322020 @default.
- W2896434232 countsByYear W28964342322021 @default.
- W2896434232 countsByYear W28964342322022 @default.
- W2896434232 countsByYear W28964342322023 @default.
- W2896434232 crossrefType "journal-article" @default.
- W2896434232 hasAuthorship W2896434232A5004917138 @default.
- W2896434232 hasAuthorship W2896434232A5019010033 @default.
- W2896434232 hasAuthorship W2896434232A5019020773 @default.
- W2896434232 hasAuthorship W2896434232A5034037577 @default.
- W2896434232 hasConcept C121332964 @default.
- W2896434232 hasConcept C127413603 @default.
- W2896434232 hasConcept C159985019 @default.
- W2896434232 hasConcept C178790620 @default.
- W2896434232 hasConcept C185592680 @default.
- W2896434232 hasConcept C192562407 @default.
- W2896434232 hasConcept C21880701 @default.
- W2896434232 hasConcept C2777516009 @default.
- W2896434232 hasConcept C2778769901 @default.
- W2896434232 hasConcept C39432304 @default.
- W2896434232 hasConcept C41952129 @default.
- W2896434232 hasConcept C537208039 @default.
- W2896434232 hasConcept C548081761 @default.
- W2896434232 hasConcept C55493867 @default.
- W2896434232 hasConcept C59427239 @default.
- W2896434232 hasConcept C82210777 @default.
- W2896434232 hasConcept C97355855 @default.
- W2896434232 hasConceptScore W2896434232C121332964 @default.
- W2896434232 hasConceptScore W2896434232C127413603 @default.
- W2896434232 hasConceptScore W2896434232C159985019 @default.
- W2896434232 hasConceptScore W2896434232C178790620 @default.
- W2896434232 hasConceptScore W2896434232C185592680 @default.
- W2896434232 hasConceptScore W2896434232C192562407 @default.
- W2896434232 hasConceptScore W2896434232C21880701 @default.
- W2896434232 hasConceptScore W2896434232C2777516009 @default.
- W2896434232 hasConceptScore W2896434232C2778769901 @default.
- W2896434232 hasConceptScore W2896434232C39432304 @default.
- W2896434232 hasConceptScore W2896434232C41952129 @default.
- W2896434232 hasConceptScore W2896434232C537208039 @default.
- W2896434232 hasConceptScore W2896434232C548081761 @default.
- W2896434232 hasConceptScore W2896434232C55493867 @default.
- W2896434232 hasConceptScore W2896434232C59427239 @default.
- W2896434232 hasConceptScore W2896434232C82210777 @default.
- W2896434232 hasConceptScore W2896434232C97355855 @default.
- W2896434232 hasFunder F4320320973 @default.
- W2896434232 hasIssue "3" @default.
- W2896434232 hasLocation W28964342321 @default.
- W2896434232 hasOpenAccess W2896434232 @default.
- W2896434232 hasPrimaryLocation W28964342321 @default.
- W2896434232 hasRelatedWork W2087432888 @default.
- W2896434232 hasRelatedWork W2369981023 @default.
- W2896434232 hasRelatedWork W2372354535 @default.
- W2896434232 hasRelatedWork W2379924063 @default.
- W2896434232 hasRelatedWork W2872669953 @default.
- W2896434232 hasRelatedWork W2899084033 @default.
- W2896434232 hasRelatedWork W2942041269 @default.
- W2896434232 hasRelatedWork W3020881974 @default.
- W2896434232 hasRelatedWork W3199386406 @default.
- W2896434232 hasRelatedWork W4213108681 @default.
- W2896434232 hasVolume "94" @default.
- W2896434232 isParatext "false" @default.
- W2896434232 isRetracted "false" @default.
- W2896434232 magId "2896434232" @default.
- W2896434232 workType "article" @default.