(19) |
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(11) |
EP 4 286 417 A8 |
(12) |
CORRECTED EUROPEAN PATENT APPLICATION |
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published in accordance with Art. 153(4) EPC |
(15) |
Correction information: |
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Corrected version no 1 (W1 A1) |
(48) |
Corrigendum issued on: |
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17.01.2024 Bulletin 2024/03 |
(43) |
Date of publication: |
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06.12.2023 Bulletin 2023/49 |
(22) |
Date of filing: 26.01.2022 |
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(51) |
International Patent Classification (IPC):
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(86) |
International application number: |
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PCT/CN2022/074012 |
(87) |
International publication number: |
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WO 2022/161400 (04.08.2022 Gazette 2022/31) |
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(84) |
Designated Contracting States: |
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AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL
NO PL PT RO RS SE SI SK SM TR |
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Designated Extension States: |
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BA ME |
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Designated Validation States: |
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KH MA MD TN |
(30) |
Priority: |
01.02.2021 CN 202110135261
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(71) |
Applicants: |
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- China Petroleum & Chemical Corporation
Beijing 100728 (CN)
- Sinopec Yangzi Petrochemical Co., Ltd.
Nanjing, Jiangsu 210048 (CN)
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(72) |
Inventors: |
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- LI, Chuanfeng
Nanjing, Jiangsu 210048 (CN)
- WANG, Wenrui
Nanjing, Jiangsu 210048 (CN)
- JING, Kun
Nanjing, Jiangsu 210048 (CN)
- CHEN, Minghua
Nanjing, Jiangsu 210048 (CN)
- XING, Yuejun
Nanjing, Jiangsu 210048 (CN)
- XIA, Huimin
Nanjing, Jiangsu 210048 (CN)
- GUO, Feng
Nanjing, Jiangsu 210048 (CN)
- YOU, Zhonglin
Nanjing, Jiangsu 210048 (CN)
- CHEN, Shaohui
Nanjing, Jiangsu 210048 (CN)
- ZHAI, Jianhong
Nanjing, Jiangsu 210048 (CN)
- YANG, Liu
Nanjing, Jiangsu 210048 (CN)
- TU, Songtao
Nanjing, Jiangsu 210048 (CN)
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(74) |
Representative: Hoffmann Eitle |
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Patent- und Rechtsanwälte PartmbB
Arabellastraße 30 81925 München 81925 München (DE) |
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(54) |
METHOD FOR CONTINUOUSLY PRODUCING ULTRA-HIGH MOLECULAR WEIGHT POLYETHYLENE BY USING
SLURRY POLYMERIZATION |
(57) The present invention relates to a process for continuously producing an ultra-high
molecular weight polyethylene by the ethylene slurry polymerization, wherein raw materials
containing ethylene and optionally at least one comonomer are subjected to a continuous
slurry polymerization in a hydrogen free atmosphere in the ethylene slurry polymerization
condition by using 2-6 ethylene slurry polymerization reaction tanks connected in
series, and the deviations of the polymerization temperatures, the polymerization
pressures, and the gas phase compositions between the tanks each other are controlled
to certain ranges. The ultra-high molecular weight polyethylene having the viscosity-average
molecular weight of 150-800 ×10
4 g/mol can be continously produced. This process has flexible polymerization manner,
large room for adjusting and controlling, and stable polymer performance. Moreover,
the obtained ultra-high molecular weight polyethylene has low metal content, low ash
content, and excellent mechanical properties.