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Synopsis and Executive Summary

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1400 1200 1000 VLE P= 1bar P= 10bar P= 50bar P=100bar P=150bar P=200bar Chapter 1 Synopsis and Executive Summary Supercritical 0 Temperature, T(°C) Fluid 1­25 50 100 150 200 250 300 350 400 450 500 800 P = 250 bar 600 400 200 Vapor Liquid Figure 1.10 Availability diagram for water. The magnitude of the availability is a direct measure of the maximum electrical work­ or power­producing potential of aqueous­produced geofluid at specific­state conditions of temperature and pressure. Availability, B (kJ/kg) The large capital investment that is contained in the well­field/reservoir portion of the system places a premium on achieving as high an efficiency as possible for a given geothermal resource, so it is worth putting considerable effort into mitigating these thermodynamic limitations. A utilization efficiency, defined as the ratio of actual net power to maximum possible power, provides a measure of how close the conversion system comes to ideal, reversible operation. Current practice for geothermal conversion systems shows utilization efficiencies typically range from 25% to 50%. Future engineering practice would like to increase these to 60% or more, which requires further investments in R&D to improve heat­transfer steps by minimizing temperature differences and increasing heat­transfer coefficients, and by improving mechanical efficiencies of converters such as turbines, turbo­expanders, and pumps. Keeping these issues in mind, the panel considered specific cases for a range of EGS resource types and applications: 1. Electricity generation using EGS geofluids from sedimentary and basement rock formations and similar reservoirs, ranging in temperature from 100°C to 400°C, including one case at supercritical conditions; 2. Electricity generation from coproduced oil and gas operations using organic binary power plant designs over resource temperatures ranging from 100°C to 180°C; 3. Combined heat and power – cogeneration of electricity and thermal energy where the conditions at the MIT COGEN plant (nominally 20 MWe and 140,000 lb/h steam) were used as a model system.

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