Team:Cornell/project/drylab/modeling/time response

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where $c(t)$ is as defined above; $\beta_1$ is 1.4 $\mu$A/day, $\beta_0$ is 2.8 $\mu$A/day, $c_{1/2}$, the half-saturating analyte concentration, is 100 $\mu$M, $\alpha$ = 0.69 day$^{-1}$; the saturating current output is $(\beta_1 + \beta_0)/\alpha$.
where $c(t)$ is as defined above; $\beta_1$ is 1.4 $\mu$A/day, $\beta_0$ is 2.8 $\mu$A/day, $c_{1/2}$, the half-saturating analyte concentration, is 100 $\mu$M, $\alpha$ = 0.69 day$^{-1}$; the saturating current output is $(\beta_1 + \beta_0)/\alpha$.
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Using this ordinary differential equation, we may numerically solve for current as a function of time&#8212;given the input function derived above. The results of such numerical solutions for various input function&#8212;performed using the differential equation solver ode45&#8212 are shown below.   
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Using this ordinary differential equation, we may numerically solve for current as a function of time&#8212;given the input function derived above. The results of such numerical solutions for various input function&#8212;performed using the differential equation solver ode45&#8212;are shown below.   

Revision as of 03:14, 26 October 2012

Time Response

Motivation

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Nam ac pulvinar felis. Mauris vitae erat at orci semper aliquet vitae quis urna. Donec sit amet tortor porttitor diam bibendum viverra. Nam dui nulla, viverra sed lacinia lobortis, ullamcorper et neque. Etiam rhoncus nibh a lacus varius vehicula convallis mi rutrum. Vestibulum vel nunc sit amet ipsum feugiat consectetur. Nulla nec ante vitae dui tristique accumsan. Morbi felis est, ornare a vestibulum vel, vulputate a eros. Nulla facilisi.

Problem Setup

Lorem ipsum dolor sit amet, consectetur adipiscing elit. Etiam sed nisl quis tellus convallis sagittis. Sed blandit metus at nulla mollis luctus. In eget turpis eros, eget lacinia sem. Curabitur ornare mauris nec lectus convallis vel ornare ligula viverra. Sed vel lectus mattis nisi auctor vestibulum vel nec ipsum. Integer pellentesque dolor lobortis elit viverra vitae vehicula dui cursus. Donec viverra, lectus eu faucibus rutrum, leo risus posuere justo, at rhoncus felis est in nibh. Pellentesque feugiat porta quam nec molestie. Morbi nunc dolor, consectetur in tempus in, hendrerit a augue. Phasellus ultrices volutpat diam vitae tincidunt. Mauris justo leo, blandit et tristique eu, lacinia in risus. Mauris elit eros, sollicitudin quis sodales quis, placerat a ante.

Nam ac pulvinar felis. Mauris vitae erat at orci semper aliquet vitae quis urna. Donec sit amet tortor porttitor diam bibendum viverra. Nam dui nulla, viverra sed lacinia lobortis, ullamcorper et neque. Etiam rhoncus nibh a lacus varius vehicula convallis mi rutrum. Vestibulum vel nunc sit amet ipsum feugiat consectetur. Nulla nec ante vitae dui tristique accumsan. Morbi felis est, ornare a vestibulum vel, vulputate a eros. Nulla facilisi.

Solution

Concentration of Analyte In Reactor
First, we need to solve for the concentration of analyte in the reactor as a function of time ($c(t)$) given an oscillating input of analyte ($[A](t)$)—with arbitrary frequency and amplitude—in the river. By performing a mass balance around the reactor (and ignoring any contribution from generation or consumption), we may write the following differential equation: $$\frac{dc}{dt} = [A](t)\cdot\frac{F}{V}-c\cdot\frac{F}{V}=D([A](t)-c),$$ $$ \mathrm{where} \ \ [A](t) = A_0\cdot\sin(2 \pi ft)+A_0,$$ and the dilution rate, $D$, equals 3.6 day$^{-1}$ for our system. Using $e^{Dt}$ as an integrating factor, we find $$c(t) = \frac{(A0 (D^2 \sin(2 \pi f t)+D^2-2 \pi D f \cos(2 \pi f t)+4 \pi^2 f^2))}{(D^2+4 \pi^2 f^2)}+k_1 e^{-D t}$$ $$ \mathrm{where} \ \ k_1 = - \frac{(A_0 (D^2-2 \pi D f+4 \pi^2))}{(D^2+4 \pi^2 f^2)} \ \ \mathrm{such\ that} \ c(0) =0 $$

Concentration of Analyte In Reactor
Now that we have an analytical solution for the concentration of analyte in the reactor over time, we wish to model the current response given the input function $c(t)$. To accomplish this, we model the time rate of change of current of our arsenic sensor using a Hill function with a cooperativity coefficient of unity—fitting data presented in Fig. X of our Current Response characterization page—and lumping all transcriptional, translational, and post-translational processes: $$\frac{dI}{dt} = \frac{\beta_1 \cdot c(t)}{c_{1/2}+c(t)}+\beta_0 - \alpha I, $$ where $c(t)$ is as defined above; $\beta_1$ is 1.4 $\mu$A/day, $\beta_0$ is 2.8 $\mu$A/day, $c_{1/2}$, the half-saturating analyte concentration, is 100 $\mu$M, $\alpha$ = 0.69 day$^{-1}$; the saturating current output is $(\beta_1 + \beta_0)/\alpha$.

Using this ordinary differential equation, we may numerically solve for current as a function of time—given the input function derived above. The results of such numerical solutions for various input function—performed using the differential equation solver ode45—are shown below.

Results: Time-Averaged Output for Rapidly Oscillating Analyte Concentrations

Lorem ipsum dolor sit amet, consectetur adipiscing elit. Etiam sed nisl quis tellus convallis sagittis. Sed blandit metus at nulla mollis luctus. In eget turpis eros, eget lacinia sem. Curabitur ornare mauris nec lectus convallis vel ornare ligula viverra. Sed vel lectus mattis nisi auctor vestibulum vel nec ipsum. Integer pellentesque dolor lobortis elit viverra vitae vehicula dui cursus. Donec viverra, lectus eu faucibus rutrum, leo risus posuere justo, at rhoncus felis est in nibh. Pellentesque feugiat porta quam nec molestie. Morbi nunc dolor, consectetur in tempus in, hendrerit a augue. Phasellus ultrices volutpat diam vitae tincidunt. Mauris justo leo, blandit et tristique eu, lacinia in risus. Mauris elit eros, sollicitudin quis sodales quis, placerat a ante.



Nam ac pulvinar felis. Mauris vitae erat at orci semper aliquet vitae quis urna. Donec sit amet tortor porttitor diam bibendum viverra. Nam dui nulla, viverra sed lacinia lobortis, ullamcorper et neque. Etiam rhoncus nibh a lacus varius vehicula convallis mi rutrum. Vestibulum vel nunc sit amet ipsum feugiat consectetur. Nulla nec ante vitae dui tristique accumsan. Morbi felis est, ornare a vestibulum vel, vulputate a eros. Nulla facilisi.

References

[1] Reference 1

[2] Reference 2

[3] Reference 3