Importance

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Abstract

Process and system for recovery of energy from geothermal brines and other hot water sources, which comprises direct contact heat exchange between the brine or hot water, and a hydrocarbon working fluid, e.g. n-butane, in a heat transfer column, the heat transfer column being operated at or above the critical pressure of the working fluid, and the hot brine or hot water feed being at a temperature at or above the critical temperature of the working fluid. The heated working fluid exiting the top of the heat transfer column is expanded through an expander to produce work. The discharge from the expander is cooled to condense working fluid which is separated in an accumulator, from condensed water vapor present in the working fluid, and the condensed working fluid is pressurized and fed back to the heat transfer column. Cooled brine or water from the bottom of the heat transfer column and water from the accumulator are fed to a flashing device such as a flash drum operated at a pressure less than that in the accumulator, and the working fluid flashed off is compressed and returned to the cooler at the expander discharge, for condensation and recovery. Uncondensible gases plus working fluid losses are vented from the accumulator. Cold brine or water is discharged from the flashing means such as the flash drum, and any scale formed in the heat transfer column is discharged from the bottom thereof. Alternatively, if the flash drum is employed as a stripping column, a portion of the vent gas from the accumulator can be recycled as stripping gas to the stripping column for recovery of working fluids therefrom. Preferably, the feed brine or hot water is degassed prior to entry into the heat transfer column, and such degassing combined with proper control of accumulator pressure provides an economic balance between energy recovery in the system and working fluid loss in the vent gas from the accumulator.

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First Claim