Unified cooling in multiple polyolefin polymerization reactors

Patent metadata

Field	Value
Publication number	US-9624316-B2
Application number	US-201615086598-A
Country	US
Kind code	B2
Filing date	Mar 31, 2016
Priority date	Apr 29, 2013
Publication date	Apr 18, 2017
Grant date	Apr 18, 2017

Abstract

A system and method for a polyolefin reactor temperature control system having a first reactor temperature control path, a second reactor temperature control path, and a shared temperature control path. The shared temperature control path is configured to combine and process coolant return streams, and to provide coolant supply for the first reactor temperature control path and the second reactor temperature control path.

First claim

What is claimed is:

1. A reactor system comprising:
a first polyolefin reactor configured to receive at least one feedstock, and at least one catalyst;
a second polyolefin reactor configured to receive at least a portion of reactor discharge from the first polyolefin reactor;
a reactor temperature control system comprising a coolant pump configured to:
provide coolant supply to the first polyolefin reactor through a first cooler and a first bypass line disposed operationally in parallel to the first cooler;
provide coolant supply to the second polyolefin reactor through a second cooler and a second bypass line disposed operationally in parallel to the second cooler; and
receive coolant return from the first polyolefin reactor and coolant return from the second polyolefin reactor; and

at least one polymer discharge on the second polyolefin reactor.

2. A reactor system comprising:
a first polyolefin reactor configured to receive at least one feedstock, and at least one catalyst;
a second polyolefin reactor configured to receive at least a portion of reactor discharge from the first polyolefin reactor;
a reactor temperature control system comprising a coolant pump configured to:
provide coolant supply to the first polyolefin reactor through a first cooler and a first bypass line disposed operationally in parallel to the first cooler;
provide coolant supply to the second polyolefin reactor through a second cooler and a second bypass line disposed operationally in parallel to the second cooler; and
receive coolant return from the first polyolefin reactor and coolant return from the second polyolefin reactor; and

at least one polymer discharge on the second polyolefin reactor,
wherein the at least one polymer discharge on the second polyolefin reactor is chosen from at least one of a continuous take-off (CTO) with a modulating valve, a continuous take-off without a modulating valve, a settling leg or a pulsating valve.

3. The reactor system of claim 2 , wherein the polymer discharge on the second polyolefin reactor is chosen from a continuous take-off with a modulating valve or a continuous take-off with an isolation valve.

4. The reactor system of claim 3 , wherein the continuous take-off controls discharge of polymer product from the second reactor thereby controlling the pressure in the second reactor; and
wherein the pressure in the second reactor controls the pressure differential between the first polyolefin reactor and the second polyolefin reactor.

5. The reactor system of claim 2 , wherein either the first or the second polyolefin reactor produces a low-molecular-weight high-density polyethylene (LMW HDPE) polymer and wherein the other polyolefin reactor produces high-molecular-weight linear-low-density polyethylene (HMW LLDPE) polymer.

6. The polyolefin reactor system of claim 1 , wherein the reactor temperature control system further comprises:
a first coolant controller configured to specify percent valve opening of a first cooler valve and percent valve opening of a first bypass valve; and
a second coolant controller configured to specify percent valve opening of a second cooler valve and percent valve opening of a second bypass valve.

7. A reactor system comprising:
a first polyolefin loop reactor operating at a first pressure;
a second polyolefin loop reactor operating at a second pressure;

wherein the pressure in the first polyolefin loop reactor floats on the pressure in the second loop reactor; and
a reactor temperature control system comprising
a coolant pump configured to
provide coolant supply to the first polyolefin loop reactor through a first cooler and a first bypass line disposed operationally in parallel to the first cooler;
provide coolant supply to the second polyolefin loop reactor through a second cooler and a second bypass line disposed operationally in parallel to the second cooler; and
receive coolant return from the first polyolefin loop reactor and coolant return from the second polyolefin loop reactor.

8. The system of claim 7 , wherein the first polyolefin loop reactor comprises a pump and the second loop reactor comprises a pump.

9. The method of claim 7 , wherein the pressure differential between an outlet of the first polyolefin loop reactor and an inlet of the second polyolefin loop reactor provides a motive force for the transfer of the slurry from the first loop reactor to the second loop reactor.

10. The reactor system of claim 7 , wherein the second polyolefin loop reactor further comprises a polymer discharge chosen from a continuous take-off with a modulating valve or a continuous take-off with an isolation valve.

11. The reactor system of claim 10 , wherein the continuous take-off controls the discharge of polymer product from the second polyolefin loop reactor thereby controlling the pressure in the second polyolefin loop reactor; and
wherein the pressure in the second polyolefin loop reactor controls the pressure differential between the first polyolefin loop reactor and the second polyolefin loop reactor.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Odi Timothy O
• Gupta Anurag
• Romig Ralph W

Classifications

• F28D15/00

  Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls {; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies (F28D17/00, F28D19/00, F28D20/00 take precedence)} · CPC title

• C08F2/01 Primary

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

• C08F2/001

  Multistage polymerisation processes characterised by a change in reactor conditions without deactivating the intermediate polymer (C08F295/00, C08F297/00 take precedence) · CPC title

• B01J2219/00094

  Jackets · CPC title

• B01J19/1862

  placed in series · CPC title