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The Incinerator Plant is output wastes incineration from Different petrochemical units. In this project we want to incinerate all output wastes from petrochemical units and also produced high pressure steam from incinerator plant heat generated.At first output waste from petrochemical collects and transfers to transit and sorting center in various forms. Input feeds of incinerator plant are shown in below table: Waste streams of petrochemical unit collect and store in Transit and Sorting Center.In Transit and Sorting Center one laboratory must be considered.In this center, waste will be classified in two groups:– Unsuitable for burning– Suitable for burningUnsuitable waste for burning can be divided into the 4 categories:– Buried materials– Materials (wastes) that need to be stabilized before buried– Materials (wastes) that can be sold.– Wastes that can be returned to petrochemical.Suitable wastes are classified into the two categories:– Input wastes to rotary kiln, consist of solids and waste fluids.– Input wastes to static kiln, consist of clean fluids and gasses.All solid wastes must be transferred to storage pit from Transit and Sorting Center. Solid wastes storage pit is input of rotary kiln.All fluid wastes must be stored and stabilized in Transit and Sorting Center. All storage and stabilization devices or facility must be considered. Storage and stabilization devices (facility) consist of:Tanks, Pumps (Transfer, Loading & Unloading), Agitator (Mixer), Blanketing System, Flare system, Instrumentation and Control Systems, etcStorage and stabilization capacity must be considered based on worst case (shut down).Generally incinerator plant consists of two similar trains (capacity of each train is 100%). Each train consists of a rotary kiln and a static kiln.Based on client request, efficiency of incinerator plant is 99.8% for all components and for aromatic must be higher than that amount.Please be attention, produce high pressure steam from output heat of incinerator plant is in this scope of work.
Secondary chamber gas residence time shall be minimum 1 second at 1050 oC.Primary Chamber:Type: Static Solid HearthMaterial of Construction: Mild Steel, 5mm thickRefractory thickness: approx.115mm thickMaterial: Refractory bricks confirming to international standard.Temperature resistance: 1400 oCInsulation thickness: approx.115mm thickMaterial: Insulation bricks confirming to international standard.Waste Charging: Manual & Automatic waste charging.Ash Removal: Manual/automaticSecondary Chamber:Type : Static Solid HearthMaterial of Construction: Mild Steel, 5mm thickRefractory thickness: approx.115mm thickMaterial: Refractory bricks confirming to international standard.Temperature resistance: 1400 oC.Insulation thickness: approx.115mmMaterial: Insulation bricks confirming to international standard.Waste Charging: Manual & Automatic waste charging.Emergency Stack:Type: cylindrical, top mounted on venturi ejector.Material of Construction: Mild Steel, 3mm thick.Refractory: 75mm thick castable.Insulation: 25mm thick castable.Quencher:Material of construction of outer body: Mild Steel refractory lined from inside.Shall have water circulation system with centrifugal pump.It shall have to reduce flue gas temperature before venturi scrubber.Shall provide pump motor of suitable capacity.Air Pollution Control Device C Venturi ScrubberType: High pressure jet type.MOC: Stainless steel C 316L.Temperature at the outlet: 78-80 oCScrubbing Media: Water with 5% causticRe- Circulation Pump for Venturi ScrubberType: CentrifugalApplication: PP/SSPiping : PPRDroplet Separator & Re-Circulation Tank (Integral)Type: CyclonicApplication: To separate water droplets from flue gasesMaterial of Construction: Mild Steel Rubber lined 3mm thickI.D. Fan:Type: High pressure centrifugalMaterial of Construction: Stainless steel 304, impeller and mild steel rubber lined castingDrive: BelCombustion Fan:Type: CentrifugalModulation: Manual damper controlMaterial of Construction: Mild SteelDrive: Direct drive