Extractive distillation
View Patent ↗A method for reducing corrosion in a diolefin extractive distillation process comprising preventing the formation of ammonium carbonate by promoting the formation of a carbonate salt that does not dissociate in the ammonium carbonate dissociation temperature range of that extractive distillation process.
1. A process wherein a diolefin selected from the group consisting of butadiene and isoprene is separated from a mixture containing at least one monoolefin, said diolefin, carbon dioxide, and ammonia using an extractive distillation step that employs a diolefin lean solvent that has a complexing affinity for said diolefin to the substantial exclusion of said at least one monoolefin, said process comprising subjecting said mixture to said extractive distillation step to form a first stream ( 4 ) containing essentially said at least one monoolefin, carbon dioxide, and ammonia and a second stream ( 5 ) containing essentially said solvent and said diolefin, said extractive distillation step being operated at a temperature at which ammonium carbonate dissociates into ammonia and carbon dioxide, cooling said first stream to a temperature at which ammonium carbonate can form from ammonia and carbon dioxide, separating a third stream ( 11 ) from said cooled first stream which third stream contains at least water and solvent, subjecting said second stream to a first thermal stripping step ( 14 ) that essentially separates said diolefin from said solvent to provide a fourth stream ( 15 ) that contains essentially said diolefin and a fifth stream ( 25 ) that contains essentially diolefin lean solvent, said first stripping step being operated at a temperature at which ammonium carbonate dissociates into ammonia and carbon dioxide, cooling said fourth stream to a temperature at which ammonium carbonate can form, separating a sixth stream ( 21 ) from said cooled fourth stream which sixth stream contains at least water and a minor amount of solvent and diolefin, subjecting at least one of said third and sixth streams to a second thermal stripping step ( 32 ) that separates solvent and hydrocarbons from water to form a seventh stream ( 33 ) containing at least solvent and hydrocarbons and a separate eighth stream ( 34 ) that contains essentially water, said second thermal stripping step being operated at a temperature at which ammonium carbonate dissociates into ammonia and carbon dioxide, cooling said seventh stream to a temperature at which ammonium carbonate can form, separating a ninth stream ( 39 ) from said cooled seventh stream which ninth stream contains at least water, solvent and hydrocarbons, returning said ninth stream as feed to said first thermal stripping step, adding to said process at least one base compound in an amount sufficient to 1) form a stable carbonate salt with carbon dioxide which stable salt will not dissociate at the operating temperatures of said extractive distillation step and said first and second thermal stripping steps, and 2) essentially exclude the formation of ammonium carbonate in said process, and removing at least part of said stable carbonate salt from said process.
2. The process of claim 1 wherein said at least one base compound is added to at least one of 1) said diolefin lean solvent before it enters said extractive distillation step, 2) said third stream, 3) said sixth stream, 4) said third and sixth streams combined, 5) said cooled seventh stream, and 7) said eighth stream.
3. The process of claim 1 wherein said stable carbonate salt is removed with a purge stream that is removed from said eighth stream.
4. The process of claim 1 wherein said eighth stream is employed as a water wash stream for said cooled first and fourth streams, the wash water from at least one of said water washes contains at least one of solvent and hydrocarbons, and said wash water is employed as feed to said second thermal stripping step along with at least one of said third and sixth streams.
5. The process of claim 1 wherein said stable carbonate salt is formed by adding at least one base compound selected from the group consisting of sodium hydroxide and potassium hydroxide.
6. The process of claim 1 wherein said at least one base compound is added to at least one process stream in an amount of from about 4 ppm to about 0.4 weight percent based on the total weight of said at least one process stream.
7. The process of claim 1 wherein said solvent tends to form ammonia under said extractive distillation conditions.
8. The process of claim 7 wherein said diolefin is butadiene, said solvent is acetonitrile.
9. The process of claim 1 wherein said temperature at which ammonium carbonate dissociates is in the range of from about 120 to about 140 F.