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. 2021 May 10;22(9):5033.
doi: 10.3390/ijms22095033.

The Quest to Quantify Selective and Synergistic Effects of Plasma for Cancer Treatment: Insights from Mathematical Modeling

Affiliations

The Quest to Quantify Selective and Synergistic Effects of Plasma for Cancer Treatment: Insights from Mathematical Modeling

Charlotta Bengtson et al. Int J Mol Sci. .

Abstract

Cold atmospheric plasma (CAP) and plasma-treated liquids (PTLs) have recently become a promising option for cancer treatment, but the underlying mechanisms of the anti-cancer effect are still to a large extent unknown. Although hydrogen peroxide (H2O2) has been recognized as the major anti-cancer agent of PTL and may enable selectivity in a certain concentration regime, the co-existence of nitrite can create a synergistic effect. We develop a mathematical model to describe the key species and features of the cellular response toward PTL. From the numerical solutions, we define a number of dependent variables, which represent feasible measures to quantify cell susceptibility in terms of the H2O2 membrane diffusion rate constant and the intracellular catalase concentration. For each of these dependent variables, we investigate the regimes of selective versus non-selective, and of synergistic versus non-synergistic effect to evaluate their potential role as a measure of cell susceptibility. Our results suggest that the maximal intracellular H2O2 concentration, which in the selective regime is almost four times greater for the most susceptible cells compared to the most resistant cells, could be used to quantify the cell susceptibility toward exogenous H2O2. We believe our theoretical approach brings novelty to the field of plasma oncology, and more broadly, to the field of redox biology, by proposing new ways to quantify the selective and synergistic anti-cancer effect of PTL in terms of inherent cell features.

Keywords: cold atmospheric plasma; hydrogen peroxide; mathematical modeling; reaction network; selective cancer treatment.

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Conflict of interest statement

The authors declare no conflict of interest. The funders had no role in the design of the study; in the collection, analyses, or interpretation of data; in the writing of the manuscript, or in the decision to publish the results.

Figures

Figure A1
Figure A1
The dependent variable c4,max (i.e., the temporal maximum of [ONOO] in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A2
Figure A2
The dependent variable c4,max (i.e., the temporal maximum of [ONOO] in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A3
Figure A3
The dependent variable τ (i.e., the system response time of [H2O2] in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A4
Figure A4
The dependent variable τ (i.e., the system response time of [H2O2] in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A5
Figure A5
The dependent variable l1 (i.e., the load of H2O2 in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A6
Figure A6
The dependent variable l1 (i.e., the load of H2O2 in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A7
Figure A7
The dependent variable l1,BS (i.e., the load over the baseline of H2O2 in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A8
Figure A8
The dependent variable l1,BS (i.e., the load over the baseline of H2O2 in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A9
Figure A9
The dependent variable l4 (i.e., the load of ONOO in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A10
Figure A10
The dependent variable l4 (i.e., the load of ONOO in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A11
Figure A11
The dependent variable s¯ (i.e., the inverse of the average rate of H2O2 consumption in the EC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A12
Figure A12
The dependent variable s¯ (i.e., the inverse of the average rate of H2O2 consumption in the EC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A13
Figure A13
The dependent variable smax (i.e., the inverse of the maximal rate of H2O2 consumption in the EC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A14
Figure A14
The dependent variable smax (i.e., the inverse of the maximal rate of H2O2 consumption in the EC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure A15
Figure A15
Illustration of a linear concentration gradient over a membrane.
Figure 1
Figure 1
Illustration of the system representing a cell exposed to PTL.
Figure 2
Figure 2
The dependent variable c1,max (i.e., the temporal maximum of [H2O2] in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 μM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure 3
Figure 3
The dependent variable c1,max (i.e., the temporal maximum of [H2O2] in the IC) as a function of kD,1 and [CATFeIII]0 when [H2O2]0EC=1 mM. [NO2]0EC=0 M (a) and [NO2]0EC=1 mM (b).
Figure 4
Figure 4
The dependent variable c1,max (i.e., the temporal maximum of [H2O2] in the IC) as a function of kD,1 and log([CATFeIII]0) when [H2O2]0EC=1 μM and [NO2]0EC=0 M.

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