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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]참가 물질
실험 절차
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.
출처 및 근거
- ORD 기록
- ord-871a3e2630eb43098b3a1ece567aec5a
- 출처 데이터셋
- uspto-grants-2014_09
- 특허 번호
- US08835706B2
연결된 노트
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