Recovery of monomers
View Patent ↗Process for the recovery of diene or vinylaromatic monomers from a gas stream, including bringing the gas stream into contact, in an extraction column (C 1 ), with an organic extraction solvent, which absorbs the monomer, and stripping or desorption with an inert gas in (C 1 ), by feeding, at the bottom of (C 1 ) below the feeding of the monomers, a stream of inert gas, a liquid stream having the extraction solvent and the monomer recovered at the bottom of (C 1 ) and an exiting gas stream recovered at the top of (C 1 ), then within a second recovery column C 2, recovery of the monomer, wherein the monomer is separated from the extraction solvent by distillation fed with the liquid stream recovered at the bottom of (C 1 ), a stream comprising concentrated monomer(s) recovered at the top of (C 2 ) and a liquid stream having the extraction solvent recovered at the bottom of (C 2 ) and then recycled to the top of (C), the monomer or monomers being dienes, vinylaromatic compounds, or isobutene.
1. A process for the recovery of one or more monomers from a gas stream, comprising the following stages:
within a first extraction column C 1 ,
a) a stage of extracting by bringing the gas stream into contact, in an extraction column (C 1 ), with an organic extraction solvent, wherein said extraction solvent absorbs said monomer or monomers, and
b) a stage of stripping or desorbing with an inert gas in the extraction column (C 1 ), by feeding, at the bottom of the column (C 1 ) and below the feeding of a gas stream laden with monomers, a stream of the inert gas,
recovering a liquid stream comprising the extraction solvent and the monomer or monomers at the bottom of the column (C 1 ) and recovering an exiting gas stream at the top of the column (C 1 ), then
within a second recovery column C 2 ,
c) a stage of recovering of said monomer or monomers, wherein said monomer or monomers are separated from the extraction solvent by distillation in a recovery column (C 2 ) fed with the liquid stream recovered at the bottom of the column (C 1 ), recovering a stream comprising concentrated monomer(s) at the top of the column (C 2 ) and recovering a liquid stream comprising the extraction solvent at the bottom of the column (C 2 ) and then recycling said liquid stream to the top of the column (C 1 ),
wherein the monomer or monomers are selected from the group consisting of dienes, vinylaromatic compounds and isobutene.
2. The process according to claim 1 , wherein the monomer or monomers are selected from the group consisting of isoprene, butadiene, isobutene and styrene.
3. The process according to claim 1 , wherein the extraction solvent is selected from the group consisting of aliphatic, cycloaliphatic and aromatic hydrocarbons having from 5 to 20 carbon atoms.
4. The process according to claim 3 , wherein the extraction solvent is selected from the group consisting of n-hexane, hexane isomer fractions, cyclohexane, n-heptane, heptane isomer fractions, methylcyclohexane and toluene.
5. The process according to claim 1 , further comprising a stage of condensation of the exiting gas stream recovered at the top of the column (C 1 ) followed by a separation stage in order to recover, on the one hand, a gas purge and, on the other hand, a solution of condensed hydrocarbons comprising extraction solvent and monomer or monomers, and recycling said solution at the top of the column (C 1 ).
6. The process according to claim 1 , further comprising heating the liquid stream comprising the extraction solvent and monomer or monomers recovered at the bottom of the column (C 1 ) in a heat exchanger E 3 by the liquid stream comprising the extraction solvent recovered at the bottom of the column (C 2 ).
7. The process according to claim 1 , further comprising a stage of condensation of the stream comprising concentrated monomer(s) recovered at the top of the column (C 2 ), followed by a separation stage in order to recover, on the one hand, noncondensable compounds and, on the other hand, a stream of monomer(s), and reinjecting a portion of the stream of monomer(s) at the top of the column (C 2 ).
8. The process according to claim 7 , further comprising recycling the noncondensable compounds at the bottom of the column (C 1 ).
9. The process according to claim 1 , further comprising subjecting the liquid stream comprising the extraction solvent and monomer or monomers recovered at the bottom of the column (C 1 ) to a separation stage in order to separate, from the said solvent, a portion of the noncondensable compounds, and reintroducing said noncondensable compounds at the bottom of the column (C 1 ).
10. The process according to claim 1 , further comprising evaporating a portion of the liquid stream comprising the extraction solvent and monomer or monomers recovered at the bottom of the column (Cl) in a heat exchanger E 6 and reintroducing this portion at the bottom of the column (C 1 ).