. 2016 Jan 13;6:953–958. doi: 10.1016/j.dib.2016.01.011

Table 1.

Comparison of some typical VOC emission/sorption mathematical models.

Model equations	Parameters	Surface sorption	Diffusion inside material	Mass transfer through the boundary layer	Reference
$\frac{d C_{g}}{d t} = N C_{i n} - N C_{g} - k_{a} C_{g} L + k_{d} C_{s} L$	k_a, k_d	+	−	−	[2]
$\frac{\partial C_{m} (x, t)}{\partial t} = D_{m} \frac{\partial^{2} C_{m} (x, t)}{\partial x^{2}}$	D_m, K_p	+	+	−	[3]
$C_{m} (0, t) = K C^{*} (t)$
$C_{m} (L, t) = 0$
$- D_{m} \frac{\partial C_{m} (x, t)}{\partial x} = h_{m} (y_{0} (t) - y (t))$	D_m, K_p,h_m	+	+	+	[4]
$V \frac{d y (t)}{d t} = A h_{m} (y_{0} (t) - y (t)) - Q y (t)$
$K = \frac{{C (x, t) \|}_{x = L}}{y_{0} (t)}$