diff --git a/Manuals/FDS_Verification_Guide/FDS_Verification_Guide.tex b/Manuals/FDS_Verification_Guide/FDS_Verification_Guide.tex
index e45e609a3ec..48be941b9af 100644
--- a/Manuals/FDS_Verification_Guide/FDS_Verification_Guide.tex
+++ b/Manuals/FDS_Verification_Guide/FDS_Verification_Guide.tex
@@ -3703,7 +3703,7 @@ \subsection{Finite Rate Reactions (\texorpdfstring{\ct{reactionrate\_arrhenius}}
 \includegraphics[trim={20pt 0pt 20pt 0pt}, clip, height=1.8in]{SCRIPT_FIGURES/reactionrate_equilibrium_species}
 \includegraphics[trim={20pt 0pt 20pt 0pt}, clip, height=1.8in]{SCRIPT_FIGURES/reactionrate_equilibrium_species_cvode}
 \end{tabular*}
-\caption[Species evolution in an equilibrium case]{Time evolution of species mass fraction for a two-step Arrhenius finite rate reaction compared to equilibrium values. The left plot is using RK2-Richardson ODE solver and the right plot is using CVODE ODE solver.}
+\caption[Species evolution in an equilibrium case]{Time evolution of species mass fraction for a two-step Arrhenius finite rate reaction compared to Cantera values. The left plot is using RK2-Richardson ODE solver and the right plot is using CVODE ODE solver.}
 \label{fig:Arrhenius_2Order_1stepb}
 \end{figure}
 
@@ -3714,7 +3714,7 @@ \subsection{Finite Rate Reactions (\texorpdfstring{\ct{reactionrate\_arrhenius}}
 \includegraphics[height=2.2in]{SCRIPT_FIGURES/reactionrate_equilibrium_temperature_cvode} &
 \includegraphics[height=2.2in]{SCRIPT_FIGURES/reactionrate_equilibrium_pressure_cvode} \\
 \end{tabular*}
-\caption[Temperature and pressure evolution for equilibrium case]{Time evolution of temperature (left) and pressure (right) for two-step Arrhenius finite rate propane reactions compared to equilibrium values. The top row is using RK2-Richardson ODE solver and the bottom row is using CVODE ODE solver.}
+\caption[Temperature and pressure evolution for equilibrium case]{Time evolution of temperature (left) and pressure (right) for two-step Arrhenius finite rate propane reactions compared to Cantera values. The top row is using RK2-Richardson ODE solver and the bottom row is using CVODE ODE solver.}
 \label{fig:Arrhenius_175Order_23stepb}
 \end{figure}
 
@@ -3757,7 +3757,7 @@ \subsection{Finite Rate Reactions (\texorpdfstring{\ct{reactionrate\_arrhenius}}
 \includegraphics[trim={20pt 0pt 20pt 0pt}, clip, height=1.8in]{SCRIPT_FIGURES/reactionrate_jones_lindstedt_species}
 \includegraphics[trim={20pt 0pt 20pt 0pt}, clip, height=1.8in]{SCRIPT_FIGURES/reactionrate_jones_lindstedt_species_cvode}
 \end{tabular*}
-\caption[Species evolution in Jones-Lindstedt case]{Time evolution of species mass fraction for a two-step Arrhenius finite rate reaction compared to equilibrium values. The left plot is using RK2-Richardson ODE solver and the right plot is using CVODE ODE solver.}
+\caption[Species evolution in Jones-Lindstedt case]{Time evolution of species mass fraction for Jones-Lindstedt four-step Arrhenius finite rate reaction compared to Cantera values. The left plot is using RK2-Richardson ODE solver and the right plot is using CVODE ODE solver.}
 \label{fig:jones_lindstedt_species}
 \end{figure}
 
@@ -3768,7 +3768,7 @@ \subsection{Finite Rate Reactions (\texorpdfstring{\ct{reactionrate\_arrhenius}}
 \includegraphics[height=2.2in]{SCRIPT_FIGURES/reactionrate_jones_lindstedt_temperature_cvode} &
 \includegraphics[height=2.2in]{SCRIPT_FIGURES/reactionrate_jones_lindstedt_pressure_cvode} \\
 \end{tabular*}
-\caption[Temperature and pressure evolution for Jones-Lindstedt case]{Time evolution of temperature (left) and pressure (right) for two-step Arrhenius finite rate propane reactions compared to equilibrium values. The top row is using RK2-Richardson ODE solver and the bottom row is using CVODE ODE solver.}
+\caption[Temperature and pressure evolution for Jones-Lindstedt case]{Time evolution of temperature (left) and pressure (right) for Jones-Lindstedt four-step Arrhenius finite rate propane reactions compared to Cantera values. The top row is using RK2-Richardson ODE solver and the bottom row is using CVODE ODE solver.}
 \label{fig:jones_lindstedt_PT}
 \end{figure}