1988
DOI: 10.1016/0026-265x(88)90035-5
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Gas-liquid chromatographic determination of the gaseous products of the two-stage pyrolysis of heavy oils

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Cited by 7 publications
(2 citation statements)
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“…In the previous papers [1][2][3][4], a two-stage pyrolysis technique using a batch-type reactor was described and was shown to be a promising method for the production of C 1 -C 4 paraffin and C 2 -C 4 olefins from the heavy residues separated from Egyptian crude oil. It has been demonstrated [5] that by adopting a contact time of $1.25 s in the second stage, an ethylene yield of 12-14 wt% can be obtained from tar-sand bitumen and 16 and 27 wt% from Tacking and Iranian heavy vacuum residues, respectively.…”
Section: Introductionmentioning
confidence: 99%
“…In the previous papers [1][2][3][4], a two-stage pyrolysis technique using a batch-type reactor was described and was shown to be a promising method for the production of C 1 -C 4 paraffin and C 2 -C 4 olefins from the heavy residues separated from Egyptian crude oil. It has been demonstrated [5] that by adopting a contact time of $1.25 s in the second stage, an ethylene yield of 12-14 wt% can be obtained from tar-sand bitumen and 16 and 27 wt% from Tacking and Iranian heavy vacuum residues, respectively.…”
Section: Introductionmentioning
confidence: 99%
“…Any processing to convert heavy ends into refined distillates should somewhere include a hydrogen addition step, heteroatom removal step. However, in the two-stage pyrolysis technique, the feed stock can be used without any pretreatment [1][2][3][4][5][6][7][8], regardless of the type of the feed stock used (contaminants are left as pyrolysis residue at the first stage) and the pyrolyzate as then contains high percentage of ethylene and propylene (≈37 wt. % unsaturated) using the normal catalyst.…”
Section: Introductionmentioning
confidence: 99%