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. 2018 Dec;127(Pt A):961-974.
doi: 10.1016/j.ijheatmasstransfer.2018.07.006. Epub 2018 Jul 14.

A continuum thermomechanical model of in vivo electrosurgical heating of hydrated soft biological tissues

Affiliations

A continuum thermomechanical model of in vivo electrosurgical heating of hydrated soft biological tissues

Wafaa Karaki et al. Int J Heat Mass Transf. 2018 Dec.

Abstract

Radio-frequency (RF) heating of soft biological tissues during electrosurgical procedures is a fast process that involves phase change through evaporation and transport of intra- and extra-cellular water, and where variations in physical properties with temperature and water content play significant role. Accurately predicting and capturing these effects would improve the modeling of temperature change in the tissue allowing the development of improved instrument design and better understanding of tissue damage and necrosis. Previous models based on the Pennes' bioheat model neglect both evaporation and transport or consider evaporation through numerical correlations, however, do not account for changes in physical properties due to mass transport or phase change, nor capture the pressure increase due to evaporation within the tissue. While a porous media approach can capture the effects of evaporation, transport, pressure and changes in physical properties, the model assumes free diffusion of liquid and gas without a careful examination of assumptions on transport parameters in intact tissue resulting in significant under prediction of temperature. These different approaches have therefore been associated with errors in temperature prediction exceeding 20% when compared to experiments due to inaccuracies in capturing the effects of evaporation losses and transport. Here, we present a model of RF heating of hydrated soft tissue based on mixture theory where the multiphase nature of tissue is captured within a continuum thermomechanics framework, simultaneously considering the transport, deformation and phase change losses due to evaporation that occur during electrosurgical heating. The model predictions are validated against data obtained for in vivo ablation of porcine liver tissue at various power settings of the electrosurgical unit. The model is able to match the mean experimental temperature data with sharp gradients in the vicinity of the electrode during rapid low and high power ablation procedures with errors less than 7.9%. Additionally, the model is able to capture fast vaporization losses and the corresponding increase in pressure due to vapor buildup which have a significant effect on temperature prediction beyond 100 °C.

Keywords: ablation; electrosurgery; mixture theory; tissue heating.

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Figures

Figure 1
Figure 1
Schematic of the in vivo experimental setup
Figure 2.
Figure 2.
Kinematics of radiofrequency activated soft tissue.
Figure 3.
Figure 3.
Finite element model of the computational domain.
Figure 4.
Figure 4.
Measured root mean square (a) current and (b) voltage for a sample measurement at 10W, 25W and 50W
Figure 5.
Figure 5.
Infrared images showing the evolution of temperature in the in vivo porcine experiments, captured at different times for sample measurements at 10W (top row), 25W (middle row) and 50W (bottom row).
Figure 6.
Figure 6.
Photographs showing electrode placement and resulting camera view occlusion.
Figure 7.
Figure 7.
Variation in mean experimental temperature (solid lines) for in the in vivo experiments compared to simulation results (dashed lines) with radial distance for (a) 10 W, (b) 25 W, (c) 50W, and with time for (d) 10 W, (e) 25 W and (f) 50W.
Figure 8.
Figure 8.
Temperature distribution in the electrode and tissue at (a) 2.160 s for 10 W, (b) 0.721 s for 25 W, and (c) 0.384 s for 50 W cases. Ratio of vapor content to initial water content (d) at 2.034 s for 10 W (e) at 0.721 s for 25 W and (f) at 0.384 s for 50 W cases.
Figure 9.
Figure 9.
Pressure distribution in the tissue at (a) 2.034 s for 10 W (b) 0.721 s for 25 W and (c) at 0.384 s for 50 W cases.
Figure 10.
Figure 10.
Variation of temporal temperature distribution in the 50W model with different values of evaporation constant K.

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