ADD a bunch of stuff about how I calculated diffusion and such
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@ -1561,7 +1561,7 @@ diffusion coefficient of \gls{stp} in water. This model was given by
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\item $D_{app}$ is the apparent diffusion rate which is equal to $D_{STP}\beta$
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\item $D_{app}$ is the apparent diffusion rate which is equal to $D_{STP}\beta$
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\item $D_{STP}$ the diffusion rate of \gls{stp} in water
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\item $D_{STP}$ the diffusion rate of \gls{stp} in water
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\item $\beta$ a fractional parameter representing the tortuousity and void
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\item $\beta$ a fractional parameter representing the tortuousity and void
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fraction of the microcarriers.
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fraction of the microcarriers (here called the `geometric diffusivity')
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\item $r$ is the interfatial radius of the unbound biotin within a microcarrier
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\item $r$ is the interfatial radius of the unbound biotin within a microcarrier
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\item $t$ is the reaction time
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\item $t$ is the reaction time
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\item $C$ is the concentration of \gls{stp} in the bulk solution
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\item $C$ is the concentration of \gls{stp} in the bulk solution
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@ -1573,18 +1573,18 @@ diffusion coefficient of \gls{stp} in water. This model was given by
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The diffusion rate of \gls{stp} was assumed to be
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The diffusion rate of \gls{stp} was assumed to be
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\SI{6.2e-7}{\cm\squared\per\second}\cite{Kamholz2001}. Since all but $\beta$ was
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\SI{6.2e-7}{\cm\squared\per\second}\cite{Kamholz2001}. Since all but $\beta$ was
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known, the experimental data was fit using these equations using
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known, the experimental data was fit using these equations using
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\inlinecode{ode45} in MATLAB and least squares as the fitting error.
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\inlinecode{ode45} in MATLAB and least squares as the fitting error. These equations were then used analogously to describe the reaction profile of
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% TODO this diffusion rate isn't actually reflected in the code
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These equations were then used analogously to describe the reaction profile of
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\glspl{mab} assuming a diffusion rate of
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\glspl{mab} assuming a diffusion rate of
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\SI{4.8e-7}{\cm\squared\per\second}\cite{Sherwood1992}.
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\SI{4.8e-7}{\cm\squared\per\second}\cite{Sherwood1992}. These same coefficients
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were used in determining the kinetics of the washing steps, and
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\SI{5.0e-6}{\cm\squared\per\second}\cite{Niether2020} was used as the diffusion
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coefficient for free biotin (which should be the only species left in solution
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after all the \gls{snb} has hydrolyzed). All diffusion coefficients were taken
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to be valid at \gls{rt} and in \gls{di} water, which is a safe assumption given
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that our reaction medium was 1X \gls{pbs}.
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% METHOD add the equation governing the washing steps
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% METHOD add the equation governing the washing steps
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The diffusion coefficient used for biotin was
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\SI{5e-6}{\cm\squared\per\second}\cite{Niether2020}
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\subsection{Luminex Analysis}\label{sec:luminex_analysis}
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\subsection{Luminex Analysis}\label{sec:luminex_analysis}
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Luminex was performed using a \product{ProcartaPlex kit}{\thermo}{custom} for
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Luminex was performed using a \product{ProcartaPlex kit}{\thermo}{custom} for
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@ -1863,10 +1863,11 @@ We observed that for either concentration, the reaction was over in
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\SIrange{20}{30}{\minute} (\cref{fig:dms_biotin_rxn_mass}). Furthermore, when
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\SIrange{20}{30}{\minute} (\cref{fig:dms_biotin_rxn_mass}). Furthermore, when
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put in terms of fraction of input \gls{snb}, we observed that the curves are
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put in terms of fraction of input \gls{snb}, we observed that the curves are
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almost identical (\cref{fig:dms_biotin_rxn_frac}). Given this, the reaction step
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almost identical (\cref{fig:dms_biotin_rxn_frac}). Given this, the reaction step
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for biotin attached was set to \SI{30}{\minute}.
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for biotin attached was set to \SI{30}{\minute}\footnote{we actually used
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\SI{60}{\minute} for most of the runs as outlined in methods, which shouldn't
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make any difference except save for being excessive according to this result}.
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% TODO these numbers might be totally incorrect
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% RESULT state how we calculated the number of stp/site
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% TODO state what the effective diffusivity is
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Next, we quantified the amount of \gls{stp} reacted with the surface of the
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Next, we quantified the amount of \gls{stp} reacted with the surface of the
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biotin-coated microcarriers. Different batches of biotin-coated \glspl{dms} were
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biotin-coated microcarriers. Different batches of biotin-coated \glspl{dms} were
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coated with \SI{40}{\ug\per\ml} \gls{stp} and sampled at intermediate timepoints
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coated with \SI{40}{\ug\per\ml} \gls{stp} and sampled at intermediate timepoints
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@ -1874,9 +1875,12 @@ using the \gls{bca} assay to indirectly quantify the amount of attached
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\gls{stp} mass. We found this reaction took approximately \SI{30}{\minute}
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\gls{stp} mass. We found this reaction took approximately \SI{30}{\minute}
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(\cref{fig:dms_stp_per_time}). Assuming a quasi-steady-state paradigm, we used
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(\cref{fig:dms_stp_per_time}). Assuming a quasi-steady-state paradigm, we used
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this experimental binding data to fit a continuous model for the \gls{stp}
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this experimental binding data to fit a continuous model for the \gls{stp}
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binding reaction. Using the diffusion rate of the \gls{stp}, we then calculated
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binding reaction. Using the diffusion rate of the \gls{stp}
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the effective diffusivity of the microcarriers to be 0.2.
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(\SI{6.2e-7}{\cm\squared\per\second}), we then calculated the geometric
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diffusivity of the microcarriers to be 0.190 (see
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\cref{eqn:stp_diffision_1,eqn:stp_diffision_2}).
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% RESULT state how I calculated the number of mab/surface area
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Using this effective diffusivity and the known diffusion coefficient of a
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Using this effective diffusivity and the known diffusion coefficient of a
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\gls{mab} protein in water, we calculated predict the binding of \glspl{mab} per
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\gls{mab} protein in water, we calculated predict the binding of \glspl{mab} per
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time onto the microcarriers (this obviously assumes that the effectively
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time onto the microcarriers (this obviously assumes that the effectively
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@ -1884,32 +1888,48 @@ diffusivity is independent of the protein used, which should be reasonable given
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that the pores of the microcarriers are huge compared to the proteins, and we
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that the pores of the microcarriers are huge compared to the proteins, and we
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don't expect any significant reaction between the protein and the microcarrier
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don't expect any significant reaction between the protein and the microcarrier
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surface save for the \gls{stp}-biotin binding reaction). According to this
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surface save for the \gls{stp}-biotin binding reaction). According to this
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model, the \gls{mab} binding reaction should be complete within \SI{15}{\minute}
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model, the \gls{mab} binding reaction should be complete within \SI{75}{\minute}
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under the conditions used for our protocol (\cref{fig:dms_mab_per_time}). Note
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under the conditions used for our protocol
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that our unoptimized coated steps were done in \SI{45}{\minute}, which seemed
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(\cref{fig:dms_mab_per_time})\footnote{We actually used \SI{60}{\minute} as
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reasonable given the slightly larger hydrodynamic radius of \glspl{mab} compared
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describe in the method section as this model was not updated with new
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to \gls{stp} which was shown to react in \SI{30}{\minute} experimentally. The
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parameters until recently; however, we should point out that even at
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results of this model should be experimentally verified.
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\SI{60}{\minute} the reaction appears to be >\SI{95}{\percent} complete}.
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% TODO find the actual numbers for this
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Finally, we calculated the number of wash steps needed to remove the reagents
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Finally, we used the effective diffusivity of the microcarriers to predict the
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between each step, including the time for each wash which required the geometric
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time needed for wash steps. This is important, as failing to wash out residual
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diffusivity of the microcarriers as calculated above. This is important, as
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free \gls{snb} (for example) could occupy binding sites on the \gls{stp}
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failing to wash out residual free \gls{snb} (for example) could occupy binding
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molecules, lowering the effective binding capacity of the \gls{mab} downstream.
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sites on the \gls{stp} molecules, lowering the effective binding capacity of the
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Once again, we assumed the microcarriers to be porous spheres, this time with an
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\gls{mab} downstream. Each wash was a 1:15 dilution (\SI{1}{\ml} reaction volume
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initial concentration of \gls{snb}, \gls{stp}, or \glspl{mab} equal to the final
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in a \SI{15}{\ml} conical tube), and in the case of \gls{snb} we wished to wash
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concentration of the bulk concentration of the previous binding step, and
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out enough biotin such that less than \SI{1}{\percent} of the binding sites in
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calculated the amount of time it would take for the concentration profile inside
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\gls{stp} would be occupied. Given this dilution factor, a maximum of
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the microcarriers to equilibrate to the bulk in the wash step. Using this model,
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\SI{20}{\nmol} of biotin remaining \cref{fig:biotin_coating} \SI{2.9}{\nmol}
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we found that the wash times for \gls{snb}, \gls{stp}, and \glspl{mab} was
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biotin binding sites on \SI{40}{\ug} \gls{stp} (assuming 4 binding sites per
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\SI{10}{\minute}, {\#} minutes, and {\#} minutes respectively. Note that
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\gls{stp} protein), this turned out to be 3 washes. By similar logic, using 2
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\gls{snb}, \gls{stp}, and \glspl{mab} each required 3, 2, and 2 washes to reduce
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washes after the \gls{stp} binding step will ensure that the number of free
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the concentration down to a level that was 1/1000 of the starting concentration
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\gls{stp} binding sites is less than 20X the number of \gls{mab} molecules
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(which was deemed to be acceptable for preventing downstream inhibition). Using
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added\footnote{This step may benefit from an additional wash, as the number of
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this in our protocol, we verified that the \gls{snb} was totally undetectable
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washes used here was develop when \SI{40}{\ug} rather than \SI{4}{\ug}
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after washing (\cref{fig:dms_biotin_washed}). The other two species need to be
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\gls{mab} was used to coat the \gls{dms}, yielding a much wider margin.
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verified, but note that the consequences of residual \gls{stp} or \gls{mab} are
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However, it is also not clear to what extent this matters, as the \gls{mab}
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far less severe than that of \gls{snb}.
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have multiple biotin molecules per \gls{mab} protein, and thus one \gls{mab}
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would require binding to several \gls{stp} molecules to be prevented from
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binding at all.}
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To determine the length of time required for each wash, we again assumed the
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microcarriers to be porous spheres, this time with an initial concentration of
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\gls{snb}, \gls{stp}, or \glspl{mab} equal to the final concentration of the
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bulk concentration of the previous binding step, and calculated the amount of
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time it would take for the concentration profile inside the microcarriers to
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equilibrate to the bulk in the wash step. Using this model, we found that the
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wash times for \gls{snb}, \gls{stp}, and \glspl{mab} was \SI{3}{\minute},
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\SI{15}{\minute}, and \SI{17}{\minute} respectively. We verified that the
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\gls{snb} was totally undetectable after washing (\cref{fig:dms_biotin_washed}).
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The other two species need to be verified in a similar manner; however, we
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should not that the washing time for both the \gls{stp} and \gls{mab} coating
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steps were \SI{30}{\minute}, which is a significant margin of safety (albeit
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one that could be optimized).
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\subsection{DMSs can efficiently expand T cells compared to beads}
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\subsection{DMSs can efficiently expand T cells compared to beads}
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