Matches in SemOpenAlex for { <https://semopenalex.org/work/W2016506051> ?p ?o ?g. }
Showing items 1 to 77 of
77
with 100 items per page.
- W2016506051 endingPage "1207" @default.
- W2016506051 startingPage "1193" @default.
- W2016506051 abstract "Since the oil crisis of 1973 considerable interest has been shown in the production of liquid fuels from alternative sources. In particular, processes utilizing coal as the feedstock have received considerable interest. These processes can be divided into indirect liquefaction, direct liquefaction and pyrolysis. This paper describes the modelling of indirect coal liquefaction processes in order to perform a consistent technical and economic assessment of the production of liquid fuels from coal and lignite, using a variety of gasification and synthesis gas conversion technologies. The technologies are modelled on a ‘step model’ basis where a step is defined as a combination of individual unit operations which together perform a significant function on the process streams, such as a methanol synthesis step or gasification and a physical gas cleaning step. Sample results of the modelling are presented to illustrate the scope of the work. These cover a representative range of gasifiers, liquid synthesis processes and products from the large number of combinations of feeds (3 alternatives), gasifiers (10 alternatives), products (6 alternatives), other technical parameters (up to 20 variables) and economic or financial parameters (17 variables), as well as possible sensitivity studies. The results have been validated by major European companies in absolute as well as comparative terms. The main results show that methanol is the most attractive fuel relative to current market prices, followed by fuel alcohol (a mixture of alcohols produced by modified Fischer-Tropsch synthesis), diesel from the Shell middle distillate synthesis process, diesel from the Mobil methanol to olefins gasoline diesel process, gasoline from the same process and finally gasoline from the Mobil methanol to gasoline process. Some products are currently economic based on typical world coal prices. There was a variation in production costs of up to 100% for most products depending on the type of gasifier chosen and specific feedstock." @default.
- W2016506051 created "2016-06-24" @default.
- W2016506051 creator A5055499548 @default.
- W2016506051 creator A5079240784 @default.
- W2016506051 date "1991-10-01" @default.
- W2016506051 modified "2023-09-24" @default.
- W2016506051 title "Economics of liquid fuels production by coal gasification" @default.
- W2016506051 cites W1975374989 @default.
- W2016506051 cites W2056647221 @default.
- W2016506051 doi "https://doi.org/10.1016/0016-2361(91)90241-2" @default.
- W2016506051 hasPublicationYear "1991" @default.
- W2016506051 type Work @default.
- W2016506051 sameAs 2016506051 @default.
- W2016506051 citedByCount "11" @default.
- W2016506051 countsByYear W20165060512012 @default.
- W2016506051 crossrefType "journal-article" @default.
- W2016506051 hasAuthorship W2016506051A5055499548 @default.
- W2016506051 hasAuthorship W2016506051A5079240784 @default.
- W2016506051 hasConcept C103697071 @default.
- W2016506051 hasConcept C105923489 @default.
- W2016506051 hasConcept C127413603 @default.
- W2016506051 hasConcept C138171918 @default.
- W2016506051 hasConcept C161790260 @default.
- W2016506051 hasConcept C178790620 @default.
- W2016506051 hasConcept C185592680 @default.
- W2016506051 hasConcept C191859794 @default.
- W2016506051 hasConcept C194439259 @default.
- W2016506051 hasConcept C202417442 @default.
- W2016506051 hasConcept C204030448 @default.
- W2016506051 hasConcept C206139338 @default.
- W2016506051 hasConcept C21880701 @default.
- W2016506051 hasConcept C24872536 @default.
- W2016506051 hasConcept C2779985886 @default.
- W2016506051 hasConcept C39432304 @default.
- W2016506051 hasConcept C512968161 @default.
- W2016506051 hasConcept C518851703 @default.
- W2016506051 hasConcept C548081761 @default.
- W2016506051 hasConceptScore W2016506051C103697071 @default.
- W2016506051 hasConceptScore W2016506051C105923489 @default.
- W2016506051 hasConceptScore W2016506051C127413603 @default.
- W2016506051 hasConceptScore W2016506051C138171918 @default.
- W2016506051 hasConceptScore W2016506051C161790260 @default.
- W2016506051 hasConceptScore W2016506051C178790620 @default.
- W2016506051 hasConceptScore W2016506051C185592680 @default.
- W2016506051 hasConceptScore W2016506051C191859794 @default.
- W2016506051 hasConceptScore W2016506051C194439259 @default.
- W2016506051 hasConceptScore W2016506051C202417442 @default.
- W2016506051 hasConceptScore W2016506051C204030448 @default.
- W2016506051 hasConceptScore W2016506051C206139338 @default.
- W2016506051 hasConceptScore W2016506051C21880701 @default.
- W2016506051 hasConceptScore W2016506051C24872536 @default.
- W2016506051 hasConceptScore W2016506051C2779985886 @default.
- W2016506051 hasConceptScore W2016506051C39432304 @default.
- W2016506051 hasConceptScore W2016506051C512968161 @default.
- W2016506051 hasConceptScore W2016506051C518851703 @default.
- W2016506051 hasConceptScore W2016506051C548081761 @default.
- W2016506051 hasIssue "10" @default.
- W2016506051 hasLocation W20165060511 @default.
- W2016506051 hasOpenAccess W2016506051 @default.
- W2016506051 hasPrimaryLocation W20165060511 @default.
- W2016506051 hasRelatedWork W1489874238 @default.
- W2016506051 hasRelatedWork W2009443901 @default.
- W2016506051 hasRelatedWork W2035836380 @default.
- W2016506051 hasRelatedWork W2048111294 @default.
- W2016506051 hasRelatedWork W2122248019 @default.
- W2016506051 hasRelatedWork W2130933612 @default.
- W2016506051 hasRelatedWork W4238303627 @default.
- W2016506051 hasRelatedWork W4282034940 @default.
- W2016506051 hasRelatedWork W89150731 @default.
- W2016506051 hasRelatedWork W2903819762 @default.
- W2016506051 hasVolume "70" @default.
- W2016506051 isParatext "false" @default.
- W2016506051 isRetracted "false" @default.
- W2016506051 magId "2016506051" @default.
- W2016506051 workType "article" @default.