Polymerization inhibitor for styrene dehydrogenation units
View Patent ↗Quinone methide derivatives such as 4-benzylidene-2,6-di-tert-butyl-cyclohexa-2,5 dienone are used to inhibit styrene monomer polymerization in the dehydrogenator portion of a styrene monomer production system. The inhibitor contacts the dehydrogenation effluent and does not partition in substantial amounts to the aqueous phase that is separated in the phase separator.
1. In a system for the production of styrene monomer by dehydrogenation of ethylbenzene in an upstream dehydrogenation unit of said system at elevated temperature and in the presence of steam wherein effluent from the dehydrogenation unit is formed that is subsequently separated in a phase separator located downstream from said dehydrogenation unit into a gaseous phase comprising hydrocarbons, an aqueous phase comprising steam condensate, and an organic phase comprising styrene monomer and unreacted ethylbenzene and wherein styrene is then distilled from said organic phase in a distillation unit located downstream from said phase separator, an improved method comprising contacting said effluent with an effective amount of a styrene monomer polymerization inhibitor (SMPI), wherein said SMPI comprises a quinone methide compound having the formula:
wherein R 1 and R 2 are independently H, C 1 to C 18 alkyl, C 5 to C 12 cycloalkyl; or C 7 to C 15 phenylalkyl, and R 3 is aryl, or aryl substituted with C 1 to C 6 alkyl, alkoxy, hydroxy, nitro, amino, carboxy or mixtures thereof.
2. Improved method as recited in claim 1 wherein from about 1–250 ppm of said SMPI is added to said dehydrogenation effluent based on 1 million parts of styrene monomer in said effluent.
3. Improved method as recited in claim 2 wherein from about 10–100 ppm of said SMPI is added to said dehydrogenation effluent based on 1 million parts of styrene monomer in said effluent.
4. Improved method as recited in claim 1 wherein said SMPI is 2,6-di-tert-butyl-4-benzylidene-cyclo-2,5-dienone.
5. Improved method as recited in claim 4 wherein said SMPI is fed into said phase separator in order to contact said dehydrogenation effluent.
6. Improved method as recited in claim 4 wherein said SMPI is fed into said system at a location at or upstream from said phase separator.
7. Improved method as recited in claim 6 wherein said dehydrogenation effluent comprises styrene monomer, unreacted ethylbenzene and water.
8. Improved method as recited in claim 5 wherein said dehydrogenation effluent comprises styrene monomer, unreacted ethylbenzene and water.
9. Improved method as recited in claim 1 further comprising contacting said effluent with an hydroxylamine present in an amount of 1–250 ppm based upon the amount of styrene monomer in said effluent.
10. Improved method as recited in claim 9 wherein said hydroxylamine is N,N-bis(hydroxypropyl) hydroxylamine (HPHA).