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In Fonderia 1 2024

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TECNICO<br />

• Portata fino a 700 m³/h<br />

• Velocità del nastro fino a 0,35 m/s<br />

• Larghezze tazze da 500 a 1.600 mm<br />

• Layout customizzabile e design espandibile<br />

• Trasportatore aperto o completamente chiuso<br />

• Nessuna generazione ed emissione di polvere<br />

di silice<br />

• Livello di rumorosità ≤ 75 dB(A)<br />

• Manutenzione ridotta e semplice<br />

• Ridotto consumo energetico.<br />

TRASPORTO TERRA<br />

Il presente lavoro mira a dimostrare l’applicabilità<br />

del trasportatore Superbelt ® B alla movimentazione<br />

della terra di fonderia. I requisiti<br />

dell’applicazione che incidono sul design del<br />

trasportatore sono:<br />

• Elevate capacità di trasporto<br />

• Temperatura della terra anche superiore ai<br />

150÷200°C<br />

• Distribuzione granulometrica della terra<br />

• Emissioni di polvere di silice cristallina respirabile<br />

L’uso delle tazze soddisfa tutti i requisiti sopra<br />

elencati. <strong>In</strong> particolare, evita il ritorno e la fuoriuscita<br />

del materiale quando l’inclinazione del<br />

nastro trasportatore supera i 18-22° |5| (Fig. 4).<br />

Fig. 4 - Sezione tipica del Superbelt ® B.<br />

Fig. 4 - Typical cross/section of Superbelt ® B.<br />

SAND TRANSPORTATION<br />

This paper aims to demonstrate the applicability<br />

of the Superbelt ® B conveyor belt to the handling<br />

of foundry sand. The application requisites<br />

that affect the design of the conveyor belt are:<br />

• High transport capacities<br />

• Sand temperature also exceeding 150÷200°C<br />

• Sand particle size distribution<br />

• Respirable crystalline silica dust emissions<br />

The use of buckets fulfils all the above requisites.<br />

<strong>In</strong> particular, it prevents the return and spillage<br />

of material when the inclination of the conveyor<br />

belt exceeds 18-22° |5| (Fig. 4).<br />

HEAT EXCHANGE CALCULATIONS<br />

Design of the Superbelt ® B conveyor belt used<br />

an approach based on one-dimensional and<br />

computational fluid dynamics (CFD) models to<br />

predict and simulate the bucket surface temperature.<br />

The stationary thermal load of the bucket belt<br />

was assessed using thermal analysis of their 3D<br />

model (Fig. 5).<br />

Based on a given bucket belt geometry and a<br />

product transported at 750°C (selected to simulate<br />

and verify the behaviour of the bucket in<br />

a worst-case scenario), thermal analysis was<br />

carried out to verify the temperature inside the<br />

buckets.<br />

Despite the high temperature of the transported<br />

product, the buckets reach a constant temperature<br />

of between 400 and 500°C. This is possible<br />

because the return section of the belt is open,<br />

so the buckets exchange heat by both radiation<br />

and natural convection with the surrounding air<br />

(Fig. 6).<br />

After completing thermal analysis on a single<br />

bucket, a simplified 3D model was prepared to<br />

study the thermal cycle of the entire conveyor<br />

belt (Fig. 7).<br />

As shown in Fig. 7, the Superbelt ® B conveyor<br />

belt consists of:<br />

• Loading point where the product enters at<br />

high temperature<br />

• Transport section to cover the distance and<br />

reach the unloading point<br />

• Unloading section in downstream machines<br />

• Return section where the buckets exchange<br />

heat<br />

The repetitive loading and unloading cycle<br />

of the buckets leads to a heat transfer that<br />

increases over time until an equilibrium is<br />

reached (Fig. 8).<br />

90<br />

<strong>In</strong> <strong>Fonderia</strong>

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