참여 물질
| 역할 | 이름 | HCID | 투입량 |
|---|
| 반응물 | Ethane | HCID 6324 | — |
| 반응물 | Propane | HCID 6334 | — |
| 반응물 | Butane | HCID 7843 | — |
| 생성물 | Ethane propane n-butane | HCID 86671268 | — |
반응 단계
The negative value recorded for % ethane conversion in Table 5 for Performance Test 6 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 5 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 53.20 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 ethane but also ethylene, propylene, propane, etc. which would likely increase the total aromatics yield to slightly more than 54 wt % based on a 100 wt % total feed to stage 1.
출처 및 근거
| DOI | 10.6084/m9.figshare.5104873.v1 |
|---|
| 특허 번호 | US08835706B2 |
|---|
| 출처 데이터셋 | uspto-grants-2014_09 |
|---|
| ORD ID | ord-80fb69036c8a47ea9354d0d3e9c92ca1 |
|---|
| 출처 메모 | uspto-grants-2014_09 |
|---|