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GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY

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GREAT NECK WATER POLLUTION CONTROL DISTRICT NASSAU COUNTY, NEW YORK MICROTURBINE INSTALLATION FEASIBILITY STUDY ( great-neck-water-pollution-control-district-nassau-county-ne )

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Supercritical Carbon Dioxide Circulated EGS Combined with IGCC in New Mexico 3.3 Model Preparation and Results 3.3.1 Model Parameters Model preparation assumed certain key assumptions: 1. Thermal equilibrium exists everywhere at all times. 2. Injection fluid is pure CO2. Although in reality, this fluid is about 90-95% CO2. 3. Dual porosity model. The porosity depends both, on pressure and temperature. There were other key assumptions such as permeability, porosity, fracture spacing, initial reservoir composition. These values were varied to compare different model results and to determine which variables the model was most sensitive to. This analysis allows for future money to be directed towards defining the variables that would affect reservoir simulation the most . The following table shows the typical parameters taken for a model: Table 1: Parameters for EGS model Parameters Values Initial formation temperature Initial formation pressure Total formation thickness Reservoir depth Matrix porosity Fracture porosity Matrix permeability Fracture permeability Fracture spacing Injector – Producer distance Injection temperature Initial water saturation Residual water saturation (Bennion D., 2007) Rock specific heat 392 oF (200 oC) 5000 psia 4921.2 ft (1500 m) 8000 ft(2439 m) 0.1 0.1 0.01 md 0.6 md 32.8 ft (10 m) 1640.4 ft (500 m) 60 oF 0.5 0.3 0.239 BTU/lb/oF (1000 J/kg/oC) Rock thermal conductivity 0.00034 BTU/ft/sec//oF (2.1 W/m/oC) Penn State University | 3.3 Model Preparation and Results 27

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