Ellesmere Port Incinerator: Difference between revisions
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The facility is based around a water-cooled [[Rotary Kiln|rotary kiln]] which rotates at between one and six revolutions per hour, giving a waste residence time of between 30 and 90 minutes at a temperature of up to 1200°C. The slag that is produced, a form of [[IBA]], flows to a water quench system to produce a inert, glass-like solid. | The facility is based around a water-cooled [[Rotary Kiln|rotary kiln]] which rotates at between one and six revolutions per hour, giving a waste residence time of between 30 and 90 minutes at a temperature of up to 1200°C. The slag that is produced, a form of [[IBA]], flows to a water quench system to produce a inert, glass-like solid. | ||
===Secondary Combustion Chamber=== | ===Secondary Combustion Chamber=== | ||
Exhaust gases from the [[Rotary Kiln|rotary kiln]] pass into the Secondary [[Combustion|combustion]] Chamber, where [[liquid waste] and oxygen is added to create a vortex. Residence time is in excess of 2 seconds, and temperatures of up to 1200°C are achieved to manage waste destruction. | Exhaust gases from the [[Rotary Kiln|rotary kiln]] pass into the Secondary [[Combustion|combustion]] Chamber, where [[liquid waste]] and oxygen is added to create a vortex. Residence time is in excess of 2 seconds, and temperatures of up to 1200°C are achieved to manage waste destruction. | ||
===Gas Cleaning and Scrubbing=== | ===Gas Cleaning and Scrubbing=== | ||
Gases from the Secondary Combustion Chamber pass into a pair of gas heat exchangers, reducing the temperature to around 800°C, followed by quenching to 80°C to minimise the production of [[wikipedia:Dioxins and dioxin-like compounds|dioxins]]. | Gases from the Secondary Combustion Chamber pass into a pair of gas heat exchangers, reducing the temperature to around 800°C, followed by quenching to 80°C to minimise the production of [[wikipedia:Dioxins and dioxin-like compounds|dioxins]]. | ||