Granted Patent B2

US 12,281,071 · App. 17/870,821 · Granted Apr 22, 2025

Inventors: Douglas S. Hubbell (Sudbury, MA); Slawomir A. Oleksy (Billerica, MA)

Assignee: T.EN Process Technology, Inc.

C07C7/00C07C7/005C07C7/05C10G31/06C10G31/08C10G2300/1096C10G2300/4012C10G2300/807C10G2400/30

Abstract

Claims (35)

1. A method for recovery of residual styrene, comprising:

recovering a hot liquid residue stream from a flash drum of a styrene monomer purification finishing system,

wherein the hot liquid residue stream comprises residual styrene, and

wherein the styrene monomer purification finishing system comprises a distillation column upstream of the flash drum;

feeding the hot liquid residue stream and a gas to a stripping vessel downstream of the flash drum to produce a vaporized styrene stream and a final liquid residue stream,

wherein the final liquid residue stream has a lower concentration of styrene than the hot liquid residue stream; and

returning the vaporized styrene stream to the distillation column to obtain a styrene monomer product.

2. The method of claim 1 , wherein the stripping vessel operates at a temperature lower than the hot liquid residue stream.

3. The method of claim 1 , wherein the gas is noncondensable at ambient temperatures and pressures.

4. The method of claim 1 , wherein the gas is steam, natural gas, nitrogen, or air.

5. The method of claim 1 , wherein the stripping vessel operates under vacuum.

6. The method of claim 1 , further comprising recycling part of the final a liquid residue stream from the bottom of the stripping vessel to a start of a styrene prefractionation system, upstream of the styrene monomer purification finishing system.

7. The method of claim 1 , wherein the final liquid residue stream leaving the stripping vessel is at a temperature between about 250° F. and 340° F.

8. The method of claim 1 , wherein feeding the gas to the stripping vessel includes at least one of (i) feeding the gas to the stripping vessel separately from the hot liquid residue stream, or (ii) feeding the gas to the hot liquid residue stream and then to the stripping vessel.

9. The method of claim 1 , wherein the feeding comprises feeding the hot liquid residue stream to the top of the stripping vessel and the gas to the bottom of the stripping vessel.

10. A method for recovery of residual styrene, comprising:

recovering a hot liquid residue stream comprising residual styrene from a flash drum of a styrene monomer purification finishing system; and

passing the hot liquid residue stream and a stripping gas to a multi-stage stripping vessel downstream of the flash drum to generate a vaporized styrene stream,

wherein the stripping gas is air.

11. The method of claim 10 , wherein the stripping gas is introduced into the multi-stage stripping vessel separately from the hot liquid residue stream.

12. The method of claim 10 , wherein the stripping gas is introduced into the hot liquid residue stream downstream of the flash drum and upstream of the multi-stage stripping vessel.

13. The method of claim 10 , wherein the styrene monomer purification finishing system further includes a distillation column, and wherein the method further comprises:

returning the vaporized styrene stream the distillation column; and

recovering a styrene monomer product from the distillation column.

14. The method of claim 13 , further comprising:

producing a final liquid residue stream from a bottom of the stripping vessel, wherein the final liquid residue stream has a lower concentration of styrene than the hot liquid residue stream feeding the multi-stage stripping vessel.

15. The method of claim 10 , further comprising:

producing a final liquid residue stream from a bottom of the stripping vessel, wherein the final liquid residue stream has a lower concentration of styrene than the hot liquid residue stream feeding the multi-stage stripping vessel.

16. A method for recovery of residual styrene, comprising:

recovering a product from a styrene prefractionation system;

passing the product as a feed to a distillation column of a styrene monomer purification finishing system;

passing a liquid bottoms stream from the distillation column to a flash drum to obtain a hot liquid residue stream comprising residual styrene;

feeding the hot liquid residue stream and air into a stripping vessel to produce a vaporized styrene stream and a final liquid residue stream,

wherein the final liquid residue stream has a lower concentration of styrene than the hot liquid residue stream; and

returning the vaporized styrene stream to the distillation column to obtain a styrene monomer product.

Assignments (2)

Continuity (1)

References Cited (11)