IP Library Granted Patent US 12708889
Granted Patent B2
US 12708889 · App. 18/216,643 · Granted Aug 18, 2026

Polyolefin production apparatus and polyolefin production method

Inventor: Satoshi Itoguchi (Ichihara, JP)
Assignee: SUMITOMO CHEMICAL COMPANY, LIMITED
B01J19/06B01J4/008B01J19/2465C08F2/01C08F2/34C08F110/00B01J2204/005
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Quick Facts
Patent No.
US 12708889
App. No.
18/216,643
Granted
Aug 18, 2026
Kind
B2
Abstract

Polyolefin powder is transferred from a gas-phase polymerization reactor to a solid-gas separator having a relatively low pressure, while an amount of monomer gas discharged from the gas-phase polymerization reactor is kept low. A polyolefin production apparatus includes a gas-phase polymerization reactor 10 that polymerizes an olefin monomer to produce polyolefin powder, a solid-gas separator 20 , a circulation pipe LC having both ends connected to the solid-gas separator, and provided with a first compressor CP 1 , a hopper 30 , a first powder-conveying pipe L 1 connecting the gas-phase polymerization reactor and the hopper, and provided with a first valve V 1 halfway, and a second powder-conveying pipe L 2 connecting an outlet of the hopper and the circulation pipe, and provided with a second valve V 2 halfway.

Claims (20)

1 . A polyolefin production apparatus comprising:

a gas-phase polymerization reactor that polymerizes an olefin monomer to produce polyolefin powder;

a solid-gas separator;

a circulation pipe having both ends connected to the solid-gas separator, and provided with only a first compressor;

a hopper;

a first powder-conveying pipe connecting the gas-phase polymerization reactor and the hopper, and provided with a first valve halfway; and

a second powder-conveying pipe connecting an outlet of the hopper and the circulation pipe, and provided with a second valve halfway.

2 . The polyolefin production apparatus according to claim 1 , wherein the first powder-conveying pipe is disposed such that an opening on a side closer to the hopper is lower in position than an opening on a side closer to the gas-phase polymerization reactor.

3 . The polyolefin production apparatus according to claim 1 , the polyolefin production apparatus further comprising a first gas-return pipe communicating the gas-phase polymerization reactor and the hopper, and provided with a third valve.

4 . The polyolefin production apparatus according to claim 1 , the polyolefin production apparatus further comprising a communication pipe communicating an upper portion of the hopper and the circulation pipe, and provided with a fourth valve.

5 . The polyolefin production apparatus according to claim 1 , the polyolefin production apparatus further comprising:

a second gas-return pipe connecting the solid-gas separator and the gas-phase polymerization reactor; and

a second compressor provided on the second gas-return pipe.

6 . The polyolefin production apparatus according to claim 5 , wherein a gas discharge rate of the first compressor is higher than a gas discharge rate of the second compressor.

7 . The polyolefin production apparatus according to claim 1 , wherein an inner diameter of the circulation pipe is 0.025 m to 0.75 m.

8 . A method for producing polyolefin by using the polyolefin production apparatus according to claim 1 , the method comprising:

polymerizing an olefin monomer in the gas-phase polymerization reactor to produce polyolefin powder;

conveying the polyolefin powder in the gas-phase polymerization reactor to a hopper;

discharging at least a portion of gas in the solid-gas separator through a circulation pipe, and then returning the portion of the gas into the solid-gas separator again; and

feeding polyolefin powder discharged from the hopper to the circulation pipe, and conveying the polyolefin powder to the solid-gas separator by causing the polyolefin powder being entrained by gas flowing through the circulation pipe.