Emission free fluff transfer system and integrated nitrogen cycle

Patent metadata

Field	Value
Publication number	US-11549748-B1
Application number	US-202117511169-A
Country	US
Kind code	B1
Filing date	Oct 26, 2021
Priority date	Oct 26, 2021
Publication date	Jan 10, 2023
Grant date	Jan 10, 2023

Abstract

A system including a hydrocarbon recovery system integrated with a fluff transfer system, the hydrocarbon recovery system comprising a purge column, a separator, a purge gas-hydrocarbon recovery unit, and a waste gas outlet line, and the fluff transfer system comprising a fluff transfer blower, and an extruder feed tank fluidly connected with the fluff transfer blower via a fluff transfer blower outlet line and fluidly connected with the purge column. The hydrocarbon recovery system can be integrated with the fluff transfer system via a purge column fluff transfer gas inlet line fluidly connecting a purge gas inlet of the purge column with the fluff transfer blower outlet line, such that a portion of the fluff transfer gas in the fluff transfer blower outlet line is introduced into the purge column as purge gas. Make-up gas to the fluff transfer system can come from the hydrocarbon recovery system.

First claim

What is claimed is:

1. A system comprising:
a hydrocarbon recovery system integrated with a fluff transfer system,
wherein the hydrocarbon recovery system comprises: 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, a fluff outlet 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, and
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 fluff transfer system comprises:
a fluff transfer blower configured to pressurize a 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, a purge column fluff outlet line, and a rotary valve, 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 hydrocarbon recovery system is integrated with the fluff transfer system via a purge column fluff transfer gas inlet line fluidly connecting at least one of the one or more purge gas inlets of the purge column with the fluff transfer blower outlet line, whereby a portion of the fluff transfer gas in the fluff transfer blower outlet line is introduced into the purge column as at least a portion of the purge gas.

2. The system of claim 1 , wherein the hydrocarbon recovery system is further integrated with the fluff transfer system via a fluff transfer system recovered purge gas line fluidly connecting the purge gas-hydrocarbon recovery unit with the fluff transfer system, whereby at least a portion of the recovered purge gas in the recovered purge gas stream can be introduced into the fluff transfer system as the fluff transfer gas.

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

4. The system of claim 1 , wherein there is no gas outlet line from the fluff transfer system other than the purge column fluff transfer gas inlet line.

5. A system comprising:
a hydrocarbon recovery system integrated with a fluff transfer system,
wherein the hydrocarbon recovery system comprises: 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 a fluff outlet 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, and
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 fluff transfer system comprises:
a fluff transfer blower configured to pressurize a 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, a purge column fluff outlet line, and a rotary valve, 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 hydrocarbon recovery system is integrated with the fluff transfer system via a fluff transfer system recovered purge gas line fluidly connecting the recovered purge gas-hydrocarbon recovery unit with the fluff transfer system, whereby at least a portion of the recovered purge gas in the recovered purge gas stream can be introduced into the fluff transfer system as the fluff transfer gas.

6. The system of claim 5 , wherein the hydrocarbon recovery system is further integrated with the fluff transfer system via a purge column fluff transfer gas inlet line fluidly connecting at least one of the one or more purge gas inlets of the purge column with the fluff transfer blower outlet line, whereby a portion of the fluff transfer gas in the fluff transfer blower outlet line can be introduced into the purge column as at least a portion of the purge gas.

7. The system of claim 6 , wherein there is no gas outlet line from the fluff transfer system other than the purge column fluff transfer gas inlet line.

8. The system of claim 5 , wherein the waste gas outlet line is connected to the purge gas-hydrocarbon recovery unit.

9. The system of claim 5 further comprising one or more fresh purge or fluff transfer gas inlet lines.

10. The system of claim 5 further comprising upstream apparatus operable to provide the wet polymer fluff to the purge column.

11. A method comprising:
in a hydrocarbon recovery system, contacting wet polymer fluff with a purge gas 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, and a recovered purge gas from the overhead stream;
introducing the purged polymer fluff to a polymer fluff transfer system, and transporting the purged polymer fluff in the fluff transfer system via circulation of a fluff transfer gas; and
integrating the hydrocarbon recovery system and the fluff transfer system by utilizing fluff transfer gas from the fluff transfer system as the purge gas in the hydrocarbon recovery system.

12. The method of claim 11 comprising further integrating the hydrocarbon recovery system and the fluff transfer system 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.

13. The method of claim 12 , comprising utilizing substantially all of the recovered purge gas from the hydrocarbon recovery system in the fluff transfer system as the fluff transfer gas.

14. The method of claim 13 further comprising extracting no gas from the fluff transfer system other than the fluff transfer gas from the fluff transfer system utilized as the purge gas in the hydrocarbon recovery system.

15. The method of claim 11 further comprising introducing fresh purge gas into the hydrocarbon recovery system, introducing fresh fluff transfer gas into the fluff transfer system, or both introducing fresh purge gas into the hydrocarbon recovery system and introducing fresh fluff transfer gas into the fluff transfer system.

16. A method comprising:
in a hydrocarbon recov

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

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

Classifications

• B65G53/60

  Devices for separating the materials from propellant gas · CPC title

• 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

• 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

• C08F10/00

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

• C08F2/01 Primary

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