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Fimre 10: Pressure inthe Gasifier Bed During the process of gasification, carbon, hydrogen, and oxygen in biomass reacts with oxygen via a series of both exothermic and endothermic reactions such as oxidation, partial oxidation, boudard, water gas shift, water gas, dry reforming, and methane reforming, occurring both concurrently and consecutivelyto produce synthesis or producer gas. Overall, the gasification process is exothermic and the heat generated is sufficient to sustain the gasification process, hence no external energy is required to runthe process. The rate of syngas produced under the previously mentioned operating conditions was 128 scfm. Also, the composition of syngas produced during this run is presented in Table 3 and has a heating value of 151.4 Btu's/scf. A portion of the the syngas thus produced was used to generate 25kW of electricity using a low Btu genset by supplementing natural gas to syngas produced. The remainder of the syngas stream was routed to he combusted through the natural gas flare. Syngas Composition Hydrogen, %Vol Carbo_n_m_ _oIn_o_x_i.de, % V ol Carbon dioxide,%Vol Methane, % Vol Syngas €EN,Btu/cu.ft. Modipcations to the Gasification System "__1 I__--.- 12.6 15.1 15.8 - _ >6 151.4 - - I PD.8360793.2 .--. -.".""A During the shakedown process, several issues were identified that had to be addressed before the unit could be operated over longer time periods. The most serious issue encountered was back flow of hot gases from the gasifier to material handling system. The backflow of hot gases heated the screw conveyers and pyrolysed the biomass in the screw conveyers making it impossible to operate the reactor over longer durations. This issue was addressed by installing two high temperature pneumatic vortex gate valves. Post installation of these valves with several 16PDF Image | THE APPLICATION OF KENTUCKY POWER
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