The equation relating the capture velocity to the geometry of lime feeder is:
{latex}
\large
$$
{{V_{ \uparrow Plate} } \over {V_c }} = 1 + {L \over S}\cos \alpha \sin \alpha
$$
{latex}
The equation of terminal velocity to the particle diameter is:
{latex}
\large
$$
V_t = {{gd_0^2 } \over {18\Phi \nu _{H_2 O} }}{{\rho _{Floc_0 } - \rho _{H_2 O} } \over {\rho _{H_2 O} }}\left( {{d \over {d_0 }}} \right)^{D_{Fractal} - 1}
$$
{latex}
The angle of inclination and laminar flow regime allows certain sized lime particles to settle back into the column and thus prevent unnecessary lime loss. Thus the primary column would be used as a storage vessel for the suspended lime bed while the slanted tube above it would allow more lime particles to settle back to the column below, making the process more economical. +(Perhaps put the design for your tube settler on another page. I would include all relevant equations and summaries in a MathCAD page. I would include the length, angle of inclination, diameter, and predicted capture velocity as well as the critical velocity of floc particles and document these values in the wiki.)+\\
The two constraints are the tube's length and the terminal velocity of the particle. This terminal velocity should be larger than the capture velocity. The length should be large enough to let the flow in the slanting tube to become a fully developed flow; the relevant criteria can be found in the [MathCad file|https://confluence.cornell.edu/pages/viewpageattachments.action?pageId=113934807&sortBy=date&highlight=ANC+mathcad.docx]\\
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