Aromatic compound recovery
View Patent ↗A method for the solvent extraction recovery of an aromatic wherein an aromatic extract is formed that contains the aromatic and non-aromatics that are both lighter than and heavier than the aromatic, analyzing at least two separate groups of lighter and heavier non-aromatics in the extract, determining from the analyses the distribution of lighter and heavier non-aromatics present and whether the aromatic product that will be recovered from the process will be too far from its predetermined maximum non-aromatic content specification, and making process changes that will cause the process to produce the aromatic product with a non-aromatic content that is closer to its predetermined maximum non-aromatic content specification.
1. In a method for recovering at least one target aromatic compound from a mixture of aromatic and non-aromatic compounds using a solvent extraction system process under operating parameters such that a solvent is employed to absorb said aromatics and produce an aromatic extract that contains primarily aromatics with minor amounts of non-aromatic impurities, said target aromatic compound being subsequently separated by distillation from said aromatic extract to form a first aromatic product that contains primarily said target aromatic compound and minor amounts of said non-aromatic impurities, said non-aromatic impurities being required to be present in said first aromatic product in amounts less than a predetermined maximum specification, the improvement comprising compositionally analyzing said aromatic extract to determine at least two separate groups of lighter and heavier boiling non-aromatics, the first group of said at least two separate groups having lighter boiling points that start with the lowest boiling point non-aromatic present in said extract, the second group of said at least two separate groups having non-aromatic boiling points higher than said first group, determining the distribution of lighter and heavier non-aromatics between said at least two groups, and adjusting said operating parameters so that said first aromatic product has a non-aromatic impurity content that is nearer to its predetermined maximum specification.
2. The method of claim 1 wherein said first group of non-aromatic impurities has a maximum boiling limit that is within at least about 25° F. of the boiling point of said target aromatic compound, and said amount of non-aromatic impurities present in said first aromatic product before said adjusting of said operating parameters is at least about 50 weight % less than said predetermined maximum specification.
3. The method of claim 1 wherein said target aromatic compound is benzene, and said first group has an upper boiling limit that is in the range of from about 10° F. below the boiling point of benzene up to about 10° F. above the boiling point of benzene.
4. The method of claim 3 wherein there is a second target aromatic compound to be produced as a second aromatic product, said second group of said two separate groups has non-aromatics that are present in said aromatic extract and are higher boiling than said first group, determining the distribution of lighter and heavier non-aromatics between said two separate groups, and changing said operating parameters so that said second aromatic product has a non-aromatic impurity content that is closer to its predetermined maximum specification for said second aromatic product.
5. The method of claim 4 wherein said second target aromatic compound is toluene, said second group of non-aromatic impurities has an upper boiling limit in the range of from about 25° F. less than the boiling point of toluene up to about 25° F. more than the boiling point of toluene, and said amount of non-aromatic impurities present in said second aromatic product before changing said operating parameters is at least about 50 wt. % less than said predetermined specification for said second product.
6. The method of claim 4 wherein said aromatic extract is additionally compositionally analyzed for at least one additional group of non-aromatic impurities that are present in said aromatic extract.
7. The method of claim 6 wherein said at least one additional target aromatic compound is selected from the group consisting of at least one xylene and ethyl benzene.
8. The method of claim 7 wherein one of said at least one additional group of non-aromatic impurities has an upper boiling limit in the range of from about 10° F. less than the boiling point of the target aromatic compound in question up to about 10° F. more than such boiling point, and said amount of non-aromatic impurities present in said at least one additional aromatic product before changing said operating parameters is at least about 50 wt. % less than the predetermined specification for said target aromatic compound in question.