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Saturday 18 February 2017

METALLURGICAL AUTOMOBILE RECYCLING PLANT

The use of cupola plant for recycling considerable quantities of steel scrap containing non-metallic material is not new. However, the use of cupola technology as the heart of an integrated reprocessing system for automobile body shells would result in a low cost bulk metal supply route for large foundry operations where there is a readily available source of suitable feedstock.
Over recent years the increasing pressures to reduce waste and improve reprocessing opportunities has resulted in many automobile manufacturers claiming a higher degree of recyclability for their products. This, together with increased use of valuable recoverable material, is likely to lead to more selective dismantling. Nevertheless, significant quantities of organic materials in the form of paints, lubricants and plastic components and the trim are likely to remain in the resulting car body shell. Zinc coated steel will almost certainly feature in the body construction, while wiring looms and electric motors may be a source of unwanted copper contamination unless removed prior to reprocessing. Car body shells can be prepared by either baling or fragmentation. Fragmentation scrap with appropriate magnetic separation and screening can be rendered clean and at adequately low levels of contamination. However, its generally small size and thin section do not make for an ideal cupola feedstock. Newer, modified cupola techniques to avoid excessive oxidation could improve this situation and lead to greater acceptability.
Baled scrap from known sources has been fairly widely used for cupola charges, although in smaller furnaces the tendency to scaffolding problems has limited its use. The use of hot blast and a tapered shell arrangement will alleviate the scaffolding difficulty and reduce oxidation problems with such feedstock.

Ancillary Equipment
Ü Environmental Control

The design of effective emission control equipment for cupolas is more difficult than for other foundry processes due to the wide range of gas temperatures (100–1200ºC), particle sizes (<1 mm to 10 mm) and flow rates involved. In addition, the presence of sulphur dioxide can cause corrosion problems and any combusted volatile matter may create condensation difficulties with filter media. The high levels of carbon monoxide can be hazardous and unacceptable from a discharge point of view unless burnt.
Most modern emission control plant for cupolas is based on the use of dry bag filter systems. Cold blast operation can result in effluent gas temperatures which vary during the campaign and are generally well in excess of that capable of being handled by economical fabric filters. Gas cooling is therefore required to prevent damage to the filter bags. However, too low a gas temperature may result in condensation of both volatile matter and water vapour leading to adverse effects on plant performance. These include blinding of the filter fabric, corrosion problems in the plant itself, and risk of fire or explosion damage due to flammable deposit ignition.
In order to heat the blast in hot blast cupolas, the off-take gases are burnt in a recuperator but the system actually used may vary depending on the condition of the gases to be handled.
Ü Dust and Waste Injection Systems
Much research and development effort has been expended over the years in attempting to perfect methods for introducing particulate materials in cupolas and these can be categorised as follows:
 exploitation of swarf and borings
 concentration of metallic elements, in particular zinc, for subsequent recovery
 recycling of waste materials such as collector waste, used sands, etc.

Most injection systems have been based on lancing systems incorporation in the tuyeres but it has been found that the cooling effect involved has restricted the opportunities for significant continuous injection because of the need to melt the material collected in the coke bed. It is, therefore, of considerable interest to increase the continuous injection rates and to establish practical feed rates for various waste materials.
Some work undertaken in Germany has been carried out using oxy-fuel burners in the tuyeres of a hot blast cupola. The technology should be transferable to most types of cupolas.
A mixture of natural gas and oxygen is supplied to the burner with dust being injected through the burner pipe from a specially designed transporter unit and ejected through the burner outlet.
Oxy-fuel burners result in very high flame temperatures compared to fuel-air systems, since no nitrogen has to be heated.
Each type of particle influences the overall melting process in a different way, for instance the carbon containing flue ash/cupola dust acts as a supplementary fuel. In these trials the injection rates were restricted by iron quality considerations rather than blockage of the coke bed in front of the tuyeres.
Other advantages of tuyere oxygen injection, such as charge coke reduction, reduced blast air requirements, better carbon pick-up and metal temperatures can be achieved by use of the burners when injection is not being employed. This makes for increased furnace flexibility. Recycling of dry bag filter dusts by cupola injection can result in the concentration of zinc such that it can be sold to a zinc reclaimer.
Ü Waste Heat Recovery

The exhaust gases leaving a cupola are at a high temperature and contain combustible elements which could be exploited as an energy source. Clearly this energy is utilised in hot blast cupolas to good effect but even in these cases less than 50% of the energy available is employed The available waste heat could be used for a variety of other applications by employing suitable heat exchanger systems. Indeed a few examples do exist of hot water and steam production for space heating and process heat. Space heating and hot water production for ablutions and other uses may not be required consistently but one interesting example of a process heat application is for steam generation to power an electricity generating set and compressor. Foundries usually require both electricity and compressed air during their operating hours and therefore there is a continuous outlet for the waste heat from the cupola plant. It is claimed that the use of this system on a 50 tonnes/hr hot blast facility results in an energy utilisation approaching 100%.
Other possible applications of cupola exit gas energy could be for charge material and coke drying and preheating duties to prevent condensation in bag filter outlet chimneys, dust extraction systems and shake-out drums.
The need for high efficiency gas cleaning equipment on modern cupola installations provides the possibility of waste heat recovery, which requires evaluation.

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