Methods and systems for upgrading mixed pyrolysis oil to light aromatics over mixed metal oxide catalysts
US-2024010934-A1 · Jan 11, 2024 · US
US9757708B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9757708-B2 |
| Application number | US-201514973443-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 17, 2015 |
| Priority date | Sep 29, 2014 |
| Publication date | Sep 12, 2017 |
| Grant date | Sep 12, 2017 |
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A lean MEG stream having a first pH level is contacted with a CO 2 -rich gas stream to yield a lean MEG product having a second different and lower pH level preferably in a range of 6.5 to 7.0. The system and method can be readily incorporated into a slipstream MEG recovery package, with a source of the lean MEG stream being a MEG regeneration section of the package. The CO 2 -rich gas could be a vented CO 2 stream from the MEG reclamation section of the package. Unlike hydrochloric and acetic acid overdosing, CO 2 overdosing of the lean MEG stream does not lead to rapid acidification of the lean MEG product to be stored or injected.
Opening claim text (preview).
What is claimed: 1. A MEG recovery system comprising a vessel for adjusting a pH level of a lean MEG stream exiting a MEG regeneration unit, the vessel including an inlet in fluid communication with the lean MEG stream and a port in fluid communication with a CO 2 -rich gas stream from a MEG reclamation unit, the lean MEG stream and the CO 2 -rich gas stream coming into contact with one another within the vessel, the vessel further including an outlet for a reduced pH lean MEG stream and a different outlet to vent a reduced CO 2 gas stream. 2. A MEG recovery system according to claim 1 wherein an amount of the CO 2 -rich gas is at least equal to a stoichiometric quantity effective for achieving a desired reduced pH level. 3. A MEG recovery system according to claim 2 wherein the amount of CO 2 -rich gas exceeds the stoichiometric quantity. 4. A MEG recovery system according to claim 1 wherein the reduced pH lean MEG stream has a pH level-of at least 6. 5. A MEG recovery system according to claim 1 wherein the reduced pH lean MEG stream has a pH level of 7. 6. A MEG recovery system according to claim 1 wherein the lean MEG stream is mixed with a second lean MEG stream having a different pH level than a pH level of the lean MEG stream. 7. A MEG recovery system according to claim 6 further comprising the second lean MEG stream contains less salt than the lean MEG stream. 8. A MEG recovery system according to claim 6 wherein the second lean MEG stream has a pH level of 7. 9. A MEG recovery system according to claim 1 wherein a portion of the lean MEG stream exiting the regeneration unit is routed to the MEG reclamation unit. 10. A MEG recovery system according to claim 1 wherein the vessel is a gas-liquid contactor. 11. A MEG recovery system comprising a gas/liquid contactor vessel including an inlet in fluid communication with a lean MEG stream exiting a MEG regeneration unit and a port in fluid communication with a CO 2 -rich gas stream from a MEG reclamation unit, the lean MEG stream and the CO 2 -rich gas stream coming into contact with one another within the gas/liquid contactor vessel, the gas/liquid contactor vessel further including an outlet for a reduced pH lean MEG stream and a different outlet to vent a reduced CO 2 gas stream.
Use of additives, e.g. for stabilisation · CPC title
by treatment giving rise to a chemical modification of at least one compound (chemisorption C07C29/76) · CPC title
Glycols, diols or their derivatives · CPC title
by absorption · CPC title
Stationary reactors without moving elements inside · CPC title
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