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sPeCIAL ArABAL - ALUMINIUM-Nachrichten – ALU-WEB.DE

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<strong><strong>ALU</strong>MINIUM</strong> INdUstry IN the GULf<br />

successful start-up of the fume treatment<br />

centre at ras Al Khair aluminium smelter<br />

J. de Weerdt, P. Klut; danieli Corus<br />

Two FTC’s were built in Ras Al Khair,<br />

Kingdom of Saudi Arabia, as part of the<br />

Ma’aden aluminium complex. These<br />

FTC’s treat the fumes of two anode<br />

bake furnaces that supply anodes to the<br />

740,000 tpy aluminium smelter. FTC 2<br />

was commissioned in October 2012 and<br />

is currently running at full capacity. The<br />

cold commissioning of FTC 1 was done<br />

in January 2013, and hot commissioning<br />

took place in June 2013. As with all startups,<br />

there were some challenges to overcome,<br />

but currently FTC 2 is fully operational<br />

and FTC 1 is running at about 50%<br />

of its capacity because not all fires at the<br />

anode bake furnace 1 are in operation<br />

yet. Both FTCs are performing satisfactory.<br />

FTC 2 performance tests have taken<br />

place in the first week of July 2013.<br />

The Ras Al Khair aluminium smelter project<br />

is a USD10.8 billion joint venture between<br />

Saudi Arabian Mining Company (Ma’aden)<br />

and Alcoa. The aim of the smelter project is<br />

to realise world’s largest and most efficient<br />

aluminium complex with a yearly capacity of<br />

740,000 tonnes. The project’s alumina refinery,<br />

aluminium smelter and rolling mill are located<br />

at Ras Al Khair, 90 km north of Jubail.<br />

The aluminium smelter consists of two potlines<br />

of 360 pots each, using AP37 technology.<br />

There are two anode bake furnaces, ABF 1<br />

having four fires and ABF 2 having three fires,<br />

that produce anodes for the potlines. Both<br />

ABF’s have their own dedicated FTC to treat<br />

the fumes from the fires. FTC 1 consists of<br />

six baghouses and four main exhaust fans (of<br />

which 3 duty and 1 standby) treating the fumes<br />

of ABF 1. FTC 2 consists of five baghouses and<br />

three main exhaust fans (of which 2 duty and<br />

1 standby) treating the fumes of ABF 2. Table<br />

1 summarises the process design data for FTC<br />

1 and FTC 2.<br />

The objective of the FTC’s is to meet the<br />

client requirements in terms of ease of operation,<br />

high online reliability, maintenance<br />

friendliness while performing to comply with<br />

the stringent local environmental legislations<br />

on airborne emissions. The fume composition<br />

and maximum emission levels are listed in<br />

Table 2.<br />

Type of pollutant<br />

the ftC design<br />

Fume composition<br />

[mg/Nm 3 ]<br />

Maximum<br />

emission<br />

[mg/Nm 3 ]<br />

Gaseous fluorides 0 <strong>–</strong> 200 < 0.5<br />

Particulate fluorides 0 <strong>–</strong> 50 < 0.6<br />

Total particulates 0 <strong>–</strong> 200 < 5.7<br />

Condensed soluble tars 0 <strong>–</strong> 200 < 1.7<br />

Table 2: Fume composition and maximum emission<br />

levels<br />

The most notable achievement in this project<br />

was the short time required for the engineering<br />

and fabrication of both FTC’s. The total time<br />

for the engineering of two complete FTC’s was<br />

only nine months, while only five month after<br />

placement of the purchase orders the first<br />

FTC 2 equipment arrived on site.<br />

Danieli Corus purchased equipment worldwide<br />

and transported it to site in order to meet<br />

the tight schedule. Despite the sometimes<br />

challenging custom clearance, availability of<br />

material within KSA, working pressure and<br />

deadlines that had to be met, all equipment<br />

arrived at site within a relatively short period<br />

of time.<br />

Furthermore, the equipment was supplied<br />

in large module delivery which had a major<br />

impact on site labour requirements since less<br />

site welding was required compared to combining<br />

a series of smaller components. Also,<br />

the complete piping system was prefabricated<br />

in order to reduce site labour required.<br />

This type of modularisation in combination<br />

with the split of responsibilities between<br />

manufacturing and the erection could only<br />

be accomplished with a detailed 3D model<br />

to avoid interferences on site. A detailed 3D<br />

model for both FTC’s was made in which the<br />

Fig. 1: Modular design, left <strong>–</strong> preassembled baghouse, right <strong>–</strong> fully fabricated cooling tower<br />

© Danieli Corus<br />

Process Variable FTC 1 FTC 2<br />

Fume volume (Am 3 /h) 245,000 180,000<br />

Fume temperature (°C) 220 220<br />

Underpressure at ABF (kPa) -2,000 -2,000<br />

Number of baghouses 6 5<br />

Number of main exhaust fans 3 + 1 2 + 1<br />

Alumina utilisation (t/hr) 6 4<br />

Table 1: FTC 1 and FTC 2 process design data<br />

Fig. 2: Modular design, left <strong>–</strong> preassembled stack section in laydown area, right <strong>–</strong> installation of preassembled<br />

stack section<br />

50 <strong><strong>ALU</strong>MINIUM</strong> · 9/2013

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