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Advanced Riedhammer Carbon Baking System - A Step ... - Sacmi

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Pit furnaces for the production of<br />

Example<br />

There is a growing demand for "larger" anodes all<br />

<strong>Riedhammer</strong> performance spectrum. This measure<br />

manufactured carbon are long-<br />

Anode production:<br />

over the world. Therefore, the increase of the furnace<br />

brings about an additional improvement of the space<br />

lived capital goods. As world market<br />

leader, the <strong>Riedhammer</strong> company<br />

in Nürnberg which has been<br />

constructing and continuously ad-<br />

Sections: 48<br />

Number of fires: 3<br />

Loading / section: 100 ta<br />

height during a general repair is often part of the<br />

economy and an increased yearly production output.<br />

vancing such plants since 1924<br />

offers also users of older furnaces<br />

the possibility to considerably improve<br />

the economic efficiency of<br />

their existing plants.<br />

The average lifetime of a closed<br />

ring pit furnace is approx. 250<br />

baking cycles. With a fire advance<br />

of 28 hours this means a durability<br />

of approx. 13 years. <strong>Riedhammer</strong><br />

has developed a patented and<br />

well-proved procedure for<br />

executing repairs and structural<br />

improvements on a closed furnace<br />

during operation. Contrary to a<br />

shutdown of the furnace for repair,<br />

1. Standard operation<br />

Fire advance: 28 h<br />

Yearly output: 93,857 tba<br />

2. Repair during operation<br />

Duration of repair (approx.): 150 days<br />

Fire advance 2 during repair: 48 h<br />

Yearly output (approx.) 3 : 77,786 tba<br />

Production loss<br />

compared to standard operation (approx.): 16,071 tba 17%<br />

3. Repair of shut down furnace<br />

Duration of repair (approx.) 1 : 150 days<br />

Fire advance: 0 h<br />

Yearly output (approx.) 3 : 55,286 tba<br />

Production loss<br />

compared to standard operation (approx.): 38,571 tba 41%<br />

Picture: Temperature homogeneity in the section<br />

TEMPERATURE HOMOGENEITY IN THE SECTION<br />

while considering all 3 axes.<br />

The temperature homogeneity on the Y-axis is<br />

achieved by:<br />

Flow and thermodynamic analyses of the flue gases<br />

in the section, e.g. in a section model and realisation<br />

of the gained knowledge by modifying the brickwork<br />

/ adapting the pit walls and fire shafts and thereby<br />

optimising the flow conditions.<br />

Due to the optimised geometry, the use of fibre-lined<br />

light weight section covers leads to a better<br />

distribution of the flue gases and thus also to an<br />

improved temperature homogeneity on the X-axis.<br />

this version offers considerable<br />

1 depending on some specific conditions; 2 typical value; 3 deviations are possible<br />

advantages:<br />

The first step towards repair or "retrofit" is a detailed process in the <strong>Riedhammer</strong> Research and<br />

inspection of the furnace. During this inventory the Development Centre.<br />

condition of the complete plant is examined, the After the evaluation definite proposals in view of<br />

scope of a possible reconstruction is determined and<br />

§ output increase,<br />

the baking process is analysed.<br />

§ temperature homogeneity and, in consequence,<br />

product quality improvement,<br />

Structural modifications of the geometry and the use<br />

§ energy saving,<br />

of improved materials have a considerable influence<br />

on the efficiency of the plant. The basis for possible § reduced operation costs and<br />

reconstruction measures are thermodynamic § improved environmental protection are<br />

examinations and developments derived from this elaborated.<br />

OUTPUT INCREASE<br />

Example<br />

Output increase by modifying the section geometry<br />

For example a brickwork<br />

modification may bring about a<br />

1. Per section<br />

Before reconstruction: 90 anodes/section resp. 82.20 t/section<br />

much more favourable "space After reconstruction: 105 anodes/section resp. 96.60 t/section<br />

utilisation" (relation between<br />

product and installed refractory<br />

2. Per year<br />

Before reconstruction: 32,850 anodes/section resp. 30,222 t/section<br />

material).<br />

After reconstruction: 38,325 anodes/section resp. 35,259 t/section<br />

Total output increase: 5,037 t/section<br />

Structural changes on the flue gas transfer bend<br />

between fire shaft and flue gas ring mains bring about<br />

more uniform and efficient flow conditions in the<br />

preheating zone and therefore also contribute to an<br />

improved temperature homogeneity on the X-axis.<br />

Picture: Light-weight section cover<br />

Burner manifolds adapted to the individual baking<br />

processes for most different heating media (natural<br />

gas, coke gas, heavy oil etc.) permit an improved<br />

temperature homogeneity in the main baking zone.<br />

This is realised by an individual control of the respective<br />

burners. Several thermocouples per cover are<br />

determining the basic figures for the process<br />

command system. The result is a favourable fuel<br />

consumption.<br />

A positive influence on the temperature homogeneity<br />

on the Z-axis can be achieved by optimising the<br />

baking profile.<br />

Picture: Flue gas transfer bend

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