Thermochemical Conversion Technologies .


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Ignition Types. Incineration (vitality recuperation through complete oxidation)Mass BurnRefuse Derived FuelPyrolysisGasificationPlasma circular segment (propelled warm change). Gasification. Halfway oxidation procedure utilizing air, immaculate oxygen, oxygen enhanced air, hydrogen, or steamProduces power, fules (methane, hydrogen, ethanol, engineered diesel), and concoction items Temperature > 1300oFMore adaptable
Transcripts
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Thermochemical Conversion Technologies

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Combustion Types Incineration (vitality recuperation through total oxidation) Mass Burn Refuse Derived Fuel Pyrolysis Gasification Plasma bend (propelled warm transformation)

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Gasification Partial oxidation prepare utilizing air, immaculate oxygen, oxygen enhanced air, hydrogen, or steam Produces power, fules (methane, hydrogen, ethanol, engineered diesel), and synthetic items Temperature > 1300 o F More adaptable than cremation, more mechanically complex than cremation or pyrolysis, more open acknowledgment

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Flexibility of Gasification

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Pyrolysis Thermal debasement of carbonaceous materials Lower temperature than gasification (750 – 1500 o F) Absence or constrained oxygen Products are pyrolitic oils and gas, strong scorch Distribution of items relies on upon temperature Pyrolysis oil utilized for (after suitable post-treatment): fluid fills, chemicals, cements, and different items. Various procedures straightforwardly combust pyrolysis gasses, oils, and burn

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Pyrolyzer—Mitsui R21

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Thermoselect (Gasification and Pyrolysis) Recovers a blend gas, utilizable glass-like minerals, metals rich in iron and sulfur from civil strong waste, business squander, mechanical waste and risky waste High temperature gasification of the natural waste constituents and direct combination of the inorganic parts. Water, salt and zinc focus are created as usable crude materials amid the procedure water treatment. No fiery remains, slag or channel tidies 100,000 tpd plant in Japan working since 1999

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Thermoselect (http://www.thermoselect.com/index.cfm)

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Fulcrum Bioenergy MSW to Ethanol Plant

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Plasma Arc Heating Technique utilizing electrical curve Used for ignition, pyrolysis, gasification, metals preparing Originally created by SKF Steel in Sweden for diminishing gas foriron producing Plasma coordinate softening reactor created by Westinghouse Plasma Corp. Additionally created for treating dangerous feedstocks (Contaminated soils, Low-level radioactive waste, Medical waste) Temperatures (> 1400 o C) adequate to slag fiery remains Plasma control utilization 200-400 kWh/ton Commercial scale offices for treating MSW in Japan

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Plasma Arc Technology in Florida Green Power Systems is proposing to construct and work a plasma circular segment office to handle 1,000 tons for each day of city strong waste (junk) in Tallahassee, Florida. Geoplasma is proposing to manufacture a comparative office for up to 3,000 tons of strong waste every day in St. Lucie County, claims 120 MW will be created Health dangers, financial matters, and specialized issues still remain

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Process Heated utilizing direct current bend plasma for high T natural waste decimation and gasification and Alternating current controlled, resistance hearing to keep up more even T dissemination in liquid shower

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Waste Incineration - Advantages Volume and weight decreased (approx. 90% vol. furthermore, 75% wt lessening) Waste diminishment is quick, no long haul residency required Destruction in seconds where LF requires 100s of years Incineration should be possible at era site Air releases can be controlled Ash buildup is typically non-putrescible, clean, dormant Small transfer territory required Cost can be counterbalanced by warmth recuperation/offer of vitality

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Waste Incineration - Disadvantages High capital cost Skilled administrators are required (especially for heater operations) Some materials are noncombustible Some material require supplemental fuel

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Waste Incineration - Disadvantages Air contaminant potential (MACT guidelines have generously diminished dioxin, WTE 19% of Hg discharges in 1995 – 90% decrease from that point forward) Volume of gas from burning is 10 x as extraordinary as other thermochemical change forms, more prominent cost for gas cleanup/contamination control Public dissatisfaction Risk forced as opposed to intentional Incineration will diminish property estimation (saw not really genuine) Distrust of government/industry capacity to direct

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Carbon and Energy Considerations Ton of waste makes 3.5 MW of vitality amid cremation (eq. to 300 kg of fuel oil) powers 70 homes Biogenic bit of waste is viewed as CO 2 nonpartisan (tree utilizes more CO 2 amid its lifecycle than discharged amid ignition) Unlike biochemical change forms, nonbiogenic CO 2 is created Should not uproot reusing

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WTE Process

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Three Ts Time Temperature Turbulence

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System Components Refuse receipt/stockpiling Refuse bolstering Grate framework Air supply Furnace Boiler

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Energy/Mass Balance Energy Loss (Radiation) Flue Gas Waste Mass Loss (unburned C in Ash)

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Flue Gas Pollutants Particulates Acid Gasses NO x CO Organic Hazardous Air Pollutants Metal Hazardous Air Pollutants

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Particulates Solid Condensable Causes Too low of a brush T (inadequate brush) Insufficient oxygen or overabundant EA (too high T) Insufficient blending or living arrangement time Too much turbulence, entrainment of particulates Control Cyclones - not compelling for evacuation of little particulates Electrostatic precipitator  Fabric Filters (baghouses) 

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Metals Removed with particulates Mercury stays volatilized Tough to expel from pipe gas Remove source or utilize initiated carbon (alongside dioxins)

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Acid Gasses From Cl, S, N, Fl in can\'t (in plastics, materials, elastic, yd squander, paper) Uncontrolled cremation - 18-20% HCl with pH 2 Acid gas scrubber (SO 2 , HCl, HFl) as a rule in front of ESP or baghouse Wet scrubber Spray dryer Dry scrubber injectors

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Nitrogen expulsion Source expulsion to maintain a strategic distance from fuel NO x generation T < 1500 F to dodge warm NO x Denox sytems - specific synergist response through infusion of alkali

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Air Pollution Control Remove certain waste segments Good Combustion Practices Emission Control Devices

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Devices Electrostatic Precipitator Baghouses Acid Gas Scrubbers Wet scrubber Dry scrubber Chemicals included slurry to kill acids Activated Carbon Selective Non-reactant Reduction

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Stoichiometric Insufficient O 2 Excess Air Role of Excess Air – Control Three Ts T Amount of Air Added

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Stoichiometric Insufficient O 2 Excess Air Role of Excess Air – Cont\'d Increasing Moisture Amount of Air Added

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Role of Excess Air – Cont\'d Stoichiometric NOx T Optimum T Range (1500 – 1800 o F) PICs/Particulates Insufficient O 2 Excess Air Amount of Air Added

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Ash Bottom Ash – recuperated from burning chamber Heat Recovery Ash – gathered in the warmth recuperation framework (heater, economizer, superheater) Fly Ash – Particulate matter expelled before sorbents Air Pollution Control Residues – generally consolidated with fly fiery debris Combined Ash – most US offices join all cinders

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Schematic Presentation of Bottom Ash Treatment

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Ash Reuse Options Construction fill Road development Landfill day by day cover Cement square generation Treatment of corrosive mine seepage

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Refuse Boiler Fabric Filter Stack Spray Dryer Tipping Floor Ash Conveyer Metal Recovery Mass Burn Facility – Pinellas County

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Overhead Crane

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Turbine Generator

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Fabric Filter

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Conclusions Combustion stays overwhelming warm innovation for MSW transformation with acknowledged upgrades in outflows Gasification and pyrolysis frameworks now in business scale operation however industry as yet rising Improved ecological information required on working frameworks Comprehensive natural or life cycle appraisals ought to be finished

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Return to Home page Updated August 2008

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