ENIP - Skikda Ethylene Complex.This consists of an ethane ethane (ĕth`ān), CH3CH3, gaseous hydrocarbon. It is a continuous-chain alkane. As a constituent of natural gas, it is used for fuel. It can be prepared by cracking and fractional distillation of petroleum. cracker producing ethylene, on stream since 1978, and downstream units. Under a contract signed in 1971, Toyo Engineering of Japan built the 120,000 t/y ethylene plant, and in 1979 brought on stream a 40,000 t/y vinyl chloride monomer (VCM VCM Vinyl Chloride Monomer VCM Variable Cylinder Management (Honda) VCM Virtual Channel Memory VCM Value Chain Management VCM Voice-Coil Motor VCM Vehicle Control Module VCM Vignette Content Management ) plant as well as a 35,000 t/y PVC PVC: see polyvinyl chloride. PVC in full polyvinyl chloride Synthetic resin, an organic polymer made by treating vinyl chloride monomers with a peroxide. unit. A 48,000 t/y low density polyethylene Low-density polyethylene (LDPE) is a thermoplastic made from oil. It was the first grade of polyethylene, produced in 1933 by Imperial Chemical Industries (ICI) using a high pressure process via free radical polymerisation [1]. (LDPE LDPE abbr. low-density polyethylene ) unit built by Snamprogetti of Italy started production in 1980. The complex now has a 10,000 t/y hydrochloric acid unit. But the ethylene plant, based on the Bloomfield process (ABB Lummus Crest, NJ), could only run at 80% of capacity by the late 1980s. In early 1988, ENIP decided to build two more plants at the complex to produce 130,000 t/y of HDPE HDPE abbr. high-density polyethylene and 70,000 t/y of plastifiers. ENIP had to expand the ethylene plant to 220,000 t/y. Stone & Webster in 1991 submitted plans to expand the plant in three phases: restoring its 120,000 t/y capacity, removing bottlenecks, and adding a 100,000 t/y capacity based on its Advanced Recovery System (ARS) - with all work to be completed in 1995. Due to delays, ENIP in 1994 set the completion date for early 1996, in time to supply the HDPE plant - and the cost of the project including the latter plant was estimated at $300m. Neither the ethylene expansion nor the HDPE plant was completed on schedule. In December 2003 ENIP awarded Invensys a $2m contract to upgrade the outdated pneumatic boiler controls and burner management system at its Skikda complex. ENIP then said that was the first of several similar control projects it planned to launch for Skikda and its Arzew complex (see down7AlgPetchFeb14-05). |
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