Emission free fluff transfer system and integrated nitrogen cycle

Patent metadata

Field	Value
Publication number	US-12203701-B2
Application number	US-202318368752-A
Country	US
Kind code	B2
Filing date	Sep 15, 2023
Priority date	Oct 26, 2021
Publication date	Jan 21, 2025
Grant date	Jan 21, 2025

Abstract

A hydrocarbon recovery system is integrated with a fluff transfer system. The hydrocarbon recovery system is configured for contacting a wet polymer fluff with a purge gas to provide a purged polymer fluff and an overhead stream, and separating a solids stream, a recovered hydrocarbon stream, and a recovered purge gas from the overhead stream. The polymer fluff transfer system is configured to receive the purged polymer fluff from the hydrocarbon recovery system and transport the purged polymer fluff in the fluff transfer system via circulation of a fluff transfer gas. The hydrocarbon recovery system and the fluff transfer system are integrated by utilizing at least a portion of the recovered purge gas from the hydrocarbon recovery system in the fluff transfer system as the fluff transfer gas and optionally utilizing fluff transfer gas from the fluff transfer system as the purge gas in the hydrocarbon recovery system.

First claim

What is claimed is:

1. A hydrocarbon recovery system comprising:
a purge column;
a separator;
a purge gas-hydrocarbon recovery unit; and
a waste gas outlet line,
wherein the purge column is configured for contact of wet polymer fluff with a purge gas, and comprises a wet polymer fluff inlet, a gas outlet for an overhead stream comprising the purge gas and entrained polymer fluff, a fluff outlet for a purged polymer fluff, and one or more purge gas inlets for the purge gas,
wherein the separator is fluidly connected with the gas outlet of the purge column and is configured to separate solids comprising recovered polymer fluff from a separator gas outlet stream comprising the purge gas and hydrocarbon,
wherein the purge gas-hydrocarbon recovery unit is fluidly connected with the separator and is configured to separate the separator gas outlet stream into a recovered hydrocarbon stream and a recovered purge gas stream,
wherein the hydrocarbon recovery system is integrated with a fluff transfer system configured for transporting the purged polymer fluff via circulation of a fluff transfer gas,

wherein the hydrocarbon recovery system is integrated with the fluff transfer system such that at least a portion of the recovered purge gas in the recovered purge gas stream is introduced into the fluff transfer system as the fluff transfer gas; and
wherein there is no gas outlet from the fluff transfer system other than an optional outlet for the fluff transfer gas in the fluff transfer system whereby a portion of the fluff transfer gas can be introduced into the purge column as at least a portion of the purge gas.

2. The hydrocarbon recovery system of claim 1 , wherein the hydrocarbon recovery system is further integrated with the fluff transfer system such that the portion of the fluff transfer gas in the fluff transfer system is introduced into the purge column as the at least the portion of the purge gas.

3. The hydrocarbon recovery system of claim 1 , wherein the waste gas outlet line is connected to the purge gas-hydrocarbon recovery unit.

4. The hydrocarbon recovery system of claim 1 , wherein the purge gas comprises nitrogen, wherein the hydrocarbon comprises isobutane, or both wherein the purge gas comprises nitrogen and the hydrocarbon comprises isobutane.

5. The hydrocarbon recovery system of claim 1 , further comprising one or more fresh purge or fluff transfer gas inlet lines.

6. The hydrocarbon recovery system of claim 5 , comprising a fresh purge gas inlet line fluidly connected with the purge column via at least one of the one or more purge gas inlets.

7. The hydrocarbon recovery system of claim 5 , comprising a fresh fluff transfer gas inlet line fluidly connected with the fluff transfer system.

8. The hydrocarbon recovery system of claim 7 , wherein the fresh fluff transfer gas inlet line is fluidly connected with the fluff transfer gas circulation line.

9. The hydrocarbon recovery system of claim 1 further comprising upstream apparatus operable to provide the wet polymer fluff to the purge column.

10. The hydrocarbon recovery system of claim 9 , wherein the upstream apparatus comprises one or more polymerization reactors.

11. A fluff transfer system configured for transporting a purged polymer fluff from a purge column via circulation of a fluff transfer gas, the fluff transfer system comprising:
a fluff transfer blower configured to pressurize the fluff transfer gas and provide a pressurized fluff transfer gas in a fluff transfer blower outlet line, and
an extruder feed tank fluidly connected with the fluff transfer blower via the fluff transfer blower outlet line and fluidly connected with the purge column via the fluff outlet, wherein the extruder feed tank comprises an extruder feed tank fluff outlet line and an extruder feed tank fluff transfer gas outlet line, wherein the extruder feed tank fluff transfer gas outlet line is fluidly connected with the fluff transfer blower via a fluff transfer gas circulation line,
wherein the fluff transfer system is integrated with a hydrocarbon recovery system, wherein the hydrocarbon recovery system comprises the purge column and is configured for contact of wet polymer fluff with the purge gas to provide the purged polymer fluff, wherein the fluff transfer system is integrated with the hydrocarbon recovery system such that at least a portion of a recovered purge gas from the hydrocarbon recovery system is introduced into the fluff transfer system as the fluff transfer gas, and wherein there is no gas outlet line from the fluff transfer system other than optionally a line via which a portion of the fluff transfer gas can be introduced into the purge column as at least a portion of the purge gas.

12. The fluff transfer system of claim 11 , wherein the fluff transfer system is further integrated with the hydrocarbon recovery system such that the portion of the fluff transfer gas is introduced into the purge column as the at least the portion of the purge gas.

13. The fluff transfer system of claim 11 , wherein the purge gas comprises nitrogen, wherein the hydrocarbon comprises isobutane, or both wherein the purge gas comprises nitrogen and the hydrocarbon comprises isobutane.

14. The fluff transfer system of claim 11 further comprising one or more fresh fluff transfer gas inlet lines fluidly connected with the fluff transfer system.

15. The fluff transfer system of claim 14 , wherein at least one of the one or more fresh fluff transfer gas inlet lines is fluidly connected with the fluff transfer gas circulation line.

16. The fluff transfer system of claim 11 further comprising upstream apparatus operable to provide the wet polymer fluff to the purge column.

17. The fluff transfer system of claim 16 , wherein the upstream apparatus comprises one or more polymerization reactors.

18. A hydrocarbon recovery system integrated with a fluff transfer system, wherein the hydrocarbon recovery system is configured for contacting a wet polymer fluff with a purge gas in a purge column to provide a purged polymer fluff and an overhead stream comprising the purge gas and entrained polymer fluff; and separating a recovered solids stream comprising the entrained polymer fluff, a recovered hydrocarbon stream comprising a hydrocarbon, and a recovered purge gas from the overhead stream; wherein the polymer fluff transfer system is configured to receive the purged polymer fluff from the hydrocarbon recovery system and transport the purged polymer fluff in the fluff transfer system via circulation of a fluff transfer gas; and wherein the hydrocarbon recovery system and the fluff transfer system are integrated by utilizing at least a portion of the recovered purge gas from the hydrocarbon recovery system in the fluff transfer system as the fluff transfer gas, wherein there is no gas outlet line from the fluff transfer system other than optionally a line via which a portion of the fluff transfer gas can be introduced into the purge column as at least the portion of the purge gas.

19. The hydrocarbon recovery system of claim 18 , wherein the fluff transfer system is further integrated with the hydrocarbon recovery system such that the portion of the fluff transfer gas is introduced into the purge column as the at least the portion of the purge gas.

20. The hydrocarbon recovery system of claim 18 , wherein the purge gas comprises nitrogen, wherein the hydrocarbon comprises isobutane, or both wherein the purge gas comprises nitrogen and the hydrocarbon comprises isobutane.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Khankal Reza
• Mancillas Enrique
• Kaur Kamaljeet
• Li Hetian

Classifications

• B01D45/16

  generated by the winding course of the gas stream {, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes} · CPC title

• B65G53/60

  Devices for separating the materials from propellant gas · CPC title

• C08F10/00

  Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title

• F26B3/02 Primary

  by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air {(F26B3/283 and F26B3/343 take precedence)} · CPC title

• C08F2/01 Primary

  characterised by special features of the polymerisation apparatus used · CPC title