【Industry Updates】CNOOC Shell’s Phase 3 ethylene project officially launched
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This post was last edited by zhoudingshengs on 2025-1-3 at 19:51. On December 3, 2024, the IMPT team for the Phase III ethylene project of CNOOC Shell held a kick-off meeting for the 1.6 million tons per year ethylene production facility at Sinopec Engineering & Construction Co., Ltd. in Beijing, marking the official launch of this largest ethylene production project under construction in China. On November 20, 2024, the first progress meeting for CNOOC Shell Huizhou Phase III ethylene project was held. On July 7, 2024, the trial ramming work for the foundation treatment area of the CNOOC Shell Huizhou Phase III ethylene project began. On February 23, 2024, the website of the Guangdong Provincial Department of Ecology and Environment published a notice regarding the acceptance of the environmental impact assessment report for the CSOP Huizhou Phase III ethylene project. The total investment for CNOOC Shell Huizhou Phase III ethylene project is approximately 52.1 billion yuan. With a 1.6 million tons per year ethylene cracking unit as the core, 18 chemical processing units, utility systems, and supporting facilities will be constructed.
CNOOC Shell Huizhou Phase III Ethylene Project has been officially launched. It is the largest ethylene production facility under construction in China, with a total investment of around 52.1 billion yuan. The project includes an ethylene cracking unit with a capacity of 1.6 million tons per year, 18 chemical processing units, as well as the corresponding utility systems and supporting facilities. .
Excuse me, which company won the bid for the instruments in this project?
Still daring to deal with ethylene – truly impressive. 16 sets of production facilities, including an ethylene plant with a capacity of 1.6 million tons per year, a butadiene extraction plant with a capacity of 305,000 tons per year, a pyrolysis gasoline hydrogenation plant with a capacity of 1.46 million tons per year, an aromatic extraction plant with a capacity of 1.1 million tons per year, an ethylene oxide-ethylene glycol (EO-EG) plant with a capacity of 645,000 tons per year, a metallocene linear low-density polyethylene (mLLDPE) plant with a capacity of 600,000 tons per year, a linear α-olefin (LAO) plant with a capacity of 400,000 tons per year, an isomerization and disproportionation (ID) plant with a capacity of 130,000 tons per year, a Shell hydroformylation (SHF) plant with a capacity of 130,000 tons per year, a polyα-olefin (PAO) plant with a capacity of 50,000 tons per year, a polypropylene (PP) plant with a capacity of 500,000 tons per year, an ethylbenzene (EB) plant with a capacity of 1 million tons per year, a styrene-propylene oxide (SM-PO) plant with capacities of 875,000/400,000 tons per year, a polyether polyol (DMC-POD) plant with a capacity of 450,000 tons per year, a polymer polyol (POP-POD) plant with a capacity of 100,000 tons per year, and an MTBE/butene-1 plant with capacities of 270,000/80,000 tons per year