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QATAR - The Shaheen Refining Project.

APS Review Downstream Trends • Sept 3, 2007 •

Technip of France in mid-2007 won the combined front-end engineering and design (FEED) and project management consultancy (PMC) package on the grassroots al-Shaheen refinery. It is the first major package awarded on the project, with Technip beating off competition from Foster Wheeler. The FEED is expected to take 12 months and construction a further three years.

The refinery will have capacity of 250,000 b/d and will process crude from the offshore al-Shaheen oilfield (see gmt10QatrFieldsSep3-07). It will produce distillates, bitumen and green coke, as well as other fuels. The project will involve installation of naphtha hydrotreaters and splitters, twin catalytic reformers, isomerisation units, distillate hydrotreaters, vacuum distillation units, hydrocrackers and fluid catalytic crackers (FCCs).

The Mesaieed Complex: Mesaieed is an industrial zone where Qatar's oil refining and petrochemicals plants are located. The refining complex consists of two plants: Mesaieed-1 was built in the 1960s and had a capacity of 12,000 b/d, which was later upgraded to 13,000 b/d. Mesaieed-2 came on stream in 1983 with a 50,000 b/d capacity which was improved and expanded in the subsequent years. With the two plants operated as a single unit including a 5,500 b/d isomerisation facility, the complex was expanded to 137,000 b/d in early 2002 by Lurgi of Germany and GS Engineering & Construction of South Korea. The FEED was done by Parsons Process Group of the US, through its UK office. Mitsui & Co. of Japan is the main offtaker of the surplus products as it has participated in the financing of the expansion (see background in Vol. 57, DT No. 10, and Vol. 61, DT No. 10).

The complex includes two plants processing stabilised but sour condensates which come from the North Field gas. One of these plants is a conversion of existing facilities. The other is a wholly new unit. Both produce middle distillates, for which local demand is expected to rise rapidly. Both plants have been on stream since late 2001.

A new 28,000 b/d FCC and a hydrotreater have cut fuel oil supply from 19,000 b/d to 3,000 b/d and raised the output of gasoline from 13,000 b/d to 50,000 b/d. The expansion has enabled the complex to produce 21,000 b/d of naphtha, raise the LPG output from 2,500 b/d to 7,500 b/d, raise jet fuel output from 9,000 to 26,000 b/d and gasoil production from 14,000 b/d to 25,000 b/d. The gasoil is with less than 0.2% sulphur.


COPYRIGHT 2007 Input Solutions Reproduced with permission of the copyright holder. Further reproduction or distribution is prohibited without permission.
Copyright 2007, Gale Group. All rights reserved. Gale Group is a Thomson Corporation Company.
NOTE: All illustrations and photos have been removed from this article.


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