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detailed programme - SIMS - Scandinavian Simulation Society

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therefore not only desirable, but necessary. The main objective in this study is to<br />

create a practical tool to evaluate the state of geothermal reservoirs and well<br />

performances using measured wellhead conditions and inverse analysis. This is to<br />

be done by coupling a wellbore simulator with a reservoir simulator. For this<br />

purpose a new wellbore simulator, called FloWell, is designed. The program<br />

TOUGH2 is used to simulate the flow in the reservoir. The inverse analysis<br />

enables continuous evaluation on estimated parameters in both FloWell and<br />

TOUGH2, such as the permeability, productivity index and the void fraction, and<br />

the measured wellhead conditions provide up to date data to model the current<br />

situation in the geothermal system. A case study involving the Reykjanes<br />

geothermal field is used to validate the wellbore simulator FloWell as well as the<br />

new coupled reservoir-wellbore simulator.<br />

Authors: Halldóra Gudmundsdottir, Magnus Thor Jonsson, Halldor Palsson.<br />

Organization: University of Iceland<br />

Session 8 - Modeling<br />

Paper 3<br />

Title: Development of a multi-level approach to model and optimise the Kalina<br />

Split Cycle<br />

Keyword: Kalina Split Cycle, Multi-Level Modelling, Process Integration<br />

Abstract: Conversion of low-grade heat to power is currently receiving significant<br />

attention, mainly due to increasing fuel prices and the motivation for the use of<br />

sustainable energy. The Kalina cycle, based on a mixture of ammonia and water<br />

as working fluid, is suitable for this purpose and exhibits higher conversion<br />

efficiencies than conventional power cycles.<br />

The split cycle technique provides a method to further increase the thermal<br />

efficiency, by reducing the entropy generation in the heat recovery steam<br />

generator. Two streams of different ammonia concentrations enter and leave the<br />

first evaporator stage at same temperatures and pressures before being mixed at<br />

the inlet of the second evaporator stage.<br />

The multidisciplinary nature of this problem requires modelling at different<br />

system levels. This paper investigates different tools and methods suitable for<br />

demonstrating the feasibility and advantages of the split cycle.<br />

The integrated model developed and presented in this paper combines three submodels<br />

using the NIST REFPROP equations of state: a mass balance model to<br />

handle the high complexity of the split cycle, a component-based model to<br />

optimise the heat exchanger operating conditions, and a process model to<br />

investigate the integration of this process into the overall thermodynamic cycle.<br />

With identical operating conditions, results show a significant increase of the net<br />

power output compared to the baseline case. It is concluded that the split cycle<br />

method could successfully be applied in other thermodynamic cycles, such as<br />

Organic Rankine Cycles.<br />

Authors: Ulrik Larsen, Tuong-Van Nguyen<br />

Organization: Technical University of Denmark

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