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A 1D mathematical model including mass, energy and momentum transport was used to describe the curves using a non-ideal gas behaviour equation.
This, however, requires both field experiments (e.g., small volume pre-job tests) and an advanced numerical simulator that couples solid and fluid transport with fracture propagation model including mass exchange between reservoir matrix and hydraulic fracture, i.e., leak-off rate.
A thermodynamic model including mass, energy and exergy balance equations are presented for each component of the DAR cycle and this model is then validated by comparison with experimental data.
A particle reaction model including mass and heat transfer has been developed to know the temperature variations produced inside the oxygen carrier particles during the cyclic reduction and oxidation reactions taking place in a chemical-looping combustion (CLC) system.
Calibration experiments are performed, and a physical model including mass transfer and reactions inside the porous electrode as well as information about the concentration boundary layer from the CFD results is set up.
Similar(55)
The model includes mass, energy and momentum balances for both particulate and gaseous phases.
The model includes mass and crystal population balances along with mutarotation and nucleation kinetics for lactose.
The model includes mass and heat transport, transport through a product layer and chemical kinetics.
The model included mass and momentum transport within the gas channels and the porous electrodes.
The model includes mass balances of oxygen and carbon, energy balances, as well as sub-models for the gas-solid flow structure, combustion, and heat transfer from the bed to both the refractory walls and to a waterwall located in the fast bed section.
Computer models, including mass flows were established for each of the systems with the goal of closing system loops to the extent possible.
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