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Ethane → Ethane propane n-butane

HRID 76912
Notes
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Reaction equation

HRID 76912 reaction equation
CC.[CH3:3][CH2:4]C.[CH3:6][CH2:7][CH2:8][CH3:9]>>[CH3:3][CH3:4].[CH3:6][CH2:7][CH3:8].[CH3:6][CH2:7][CH2:8][CH3:9]
ParticipantsProcedureSources & evidenceReaction notes

Participants

4

Reactant 3

HCID 6324Ethane3×HCID 6334PropaneHCID 7843Butane

Product 1

HCID 86671268Ethane propane n-butane

Procedure

The negative value recorded for % ethane conversion in Table 7 for Performance Test 7 indicates that the amount of ethane made as a byproduct of propane and/or butane conversion exceeded the amount of ethane converted in this test. Nevertheless, it can be seen from Table 7 that the one stage method produced 49.57 wt % total aromatics from the given ethane/propane/n-butane feedstock, while the two stage method produced 55.50 wt % total aromatics based on a 100 wt % total feed to stage 1 followed by stage 2 which is fed with the ethane from stage 1. In a true two stage operation, it is likely that the feed to stage 2 would include all non-aromatics from the outlet of stage 1 except the fuel gas (methane and hydrogen). These non-aromatics would include not only unconverted ethane but also ethylene, propylene, propane, etc. which would likely increase the total aromatics yield to slightly more than 56 wt % based on a 100 wt % total feed to stage 1.

Sources & evidence

ORD record
ord-871a3e2630eb43098b3a1ece567aec5a
Source dataset
uspto-grants-2014_09
DOI
10.6084/m9.figshare.5104873.v1
Patent number
US08835706B2

Reaction notes

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On this pageParticipantsProcedureSources & evidenceReaction notes