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IDENTIFYING ENVIRONMENTALLY PREFERABLE USES FOR BIOMASS

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IDENTIFYING ENVIRONMENTALLY PREFERABLE USES FOR BIOMASS ( identifying-environmentally-preferable-uses-for-biomass )

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BC Bugwood Envirochem Services Inc. Figure 4.6.3 Figure 4.6.4 Figure 4.6.5 Figure 4.6.6 Figure 4.6.7 Figure 4.6.8 Figure 4.6.9 Figure4.6.10 Figure4.6.11 Figure4.6.12 Figure 4.7.1 Figure 4.7.2 Figure 4.7.3 Figure 4.7.4 Figure 4.7.5 Figure 4.7.6 Figure 4.7.7 Figure 5.1.1 Figure 5.1.2 Figure 5.2.1 Figure 5.2.2 Figure 5.2.3 Simplified Representation of the Torrefaction Process ....................................... 61 A Gasifier by Vidir Machine Inc. This Stationary Gasifier Unit Could Easily be Converted Into a Mobile Unit...............................................................................62 Counter-Current Fixed-Bed Gasifier from MESH Technologies Inc. ................... 62 Gasifier Schematics and Corresponding Temperature Profiles .......................... 64 Typical Syngas Cleaning Schematic ................................................................... 66 Syngas Material and Process Flow ..................................................................... 67 Torrefaction Material and Process Flow .............................................................. 68 EnergyBalanceofMobileandStationaryMethanolPlantfortheDirect Fluidized Gasification Option............................................................................... 69 EnergyBalanceofStationaryMethanolPlantOptionsWithandWithoutH2 Generation........................................................................................................... 69 GHGEmissionsforVariousGasifierStrategiesWithandWithoutHydrogen Generation........................................................................................................... 72 Possible Options for the Use of Wood-gas.......................................................... 73 Gas Composition as a Function of Wood Feedstock Moisture............................ 74 Flow Diagram for the Battelle Indirect Wood Gasification and Methanation Process ............................................................................................................... 75 Energy Balance of Wood Conversion to SNG ..................................................... 77 Major Natural Gas Pipelines in Western Canada ................................................ 77 Pacific Northern Gas (left) and Duke Energy (right) Pipelines ............................ 78 GHG Emissions and Emission Reductions from SNG Production ...................... 79 Comparison of the Original Feedstock Energy Contained in Products and Energy Consumed for Harvesting, Processing and Transportation .................... 80 Processing Efficiency Comparison (All Energy Outputs Over All Energy Inputs, HHV Basis)..........................................................................................................81 Comparison of Plant Economics at a Harvesting Cost of $68.55/bdt (left bars) and $40/m3 (right bars)........................................................................................84 Feedstock Incentive Required to Generate 10% ROI for Different Technologies at Harvesting Cost of $68.55/bdt (left bars) and $40/m3 (right bars) .................................................................................................................... 84 GHG Process Emissions and Displacements ..................................................... 85 Page viii

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