NIGERIA - Phase Two.Originally scheduled for completion in 1987, the 330,000 t/y ethylene complex under Phase Two came on stream in June 1995, together with a unit with the capacity to produce 90,000 t/y of propylene propylene /pro·pyl·ene/ (pro´pi-len) a gaseous hydrocarbon, CH3CHdbondCH2. propylene glycol a colorless viscous liquid used as a humectant and solvent in pharmaceutical preparations. and 22,000 t/y of butene-1. The 250,000 t/y swing plant to produce HDPE HDPE abbr. high-density polyethylene and/or LLDPE LLDPE Linear Low Density Polyethylene came on stream in late 1995, along with an 80,000 t/y PP plant. The complex is at Eleme near Port Harcourt Port Harcourt (här`kərt, –kôrt), city (1991 est. pop. 362,000), SE Nigeria, a deepwater port on the Bonny River in the Niger delta. , the site of Nigeria's oldest oil refinery in Rivers State. It is operated by Eleme Petrochemicals Co. Delays in completing the complex were largely due to heavy debts owed by the government to French and Japanese contractors working on the plant. NNPC NNPC Nigerian National Petroleum Corporation NNPC Nigerian National Petroleum Company said in 1995 the complex will satisfy domestic demand as well as provide the state with $100m per annum Per annum Yearly. in export revenues. In addition, Phase Two saved the country some $122m through import substitution. But now, income from the Eleme complex is a fraction of what was expected in the 1990s. Nigeria's Phase Two Petrochemical Plants PRODUCT CAPACITY Ethylene 330,000 t/y Propylene 90,000 t/y Butene -122,000 t/y Polypropylene 80,000 t/y Polyethylenes (HDPE, LDPE, LLDPE) 250,000 t/y Delays in production by these plants in 1995 were also caused by damage to the NGL NGL - A dialect of IGL. extraction facility at Port Harcourt from an explosion earlier in the year. Agip, operating the extraction plant, resumed normal operations in late 1995. The complex requires about 17,000 b/d of NGL. But unrest in the area in recent months has also affected the operations of these plants. Du Pont Canada handled the engineering work and supervised the construction of the LLDPE/HDPE units, under a contract signed in October 1988. Institut Francais du Petrole (IFP (1) (Intelligent Forms Processing) Using advanced techniques to scan documents and determine their data content. See ICR. (2) (Integer Factorization Problem) The difficulty of finding prime numbers in an encryption key. ) provided the process licence for the butene-1 plant. (Butene-1 is the base for LLDPE). Preliminary designs were done by Spie Batignolles of France, Technimont of Italy, and Chiyoda and Kobe Steel of Japan. M.W. Kellogg of the US was also involved as a contractor. Initially, Phase Two was criticised as being economically unviable because projections of domestic consumption levels indicated that only 60% of the planned output would be absorbed while export prospects would be limited. However, in August 1987, a World Bank financed study conducted by the Standford Research Institute of California recommended the development of Phase Two as planned, with emphasis on ethylene, polyethylene and polypropylene. |
|
||||||||||||

Printer friendly
Cite/link
Email
Feedback
Reader Opinion