A sequencing batch reactor treatment system is to be designed for a wastewater flow of $0\mathrm{.}5$ MGD with influent BOD concentration of $\backslash (260\backslash$mathrm$\{$mg$\}/\backslash$mathrm$\{$L$\}\backslash ).$ A design $\backslash (\backslash$mathrm$\{$F$\}/\backslash$mathrm$\{$M$\}\backslash )$ of $0\mathrm{.}08$ lb BOD$/$day$/$lb MLVSS$,$ waste activated sludge $($WAS$)$ concentration of $\backslash (9,000\backslash$mathrm$\{$mg$\}/\backslash$mathrm$\{$L$\}\backslash )($i$.$e$.$ MLSS$),$ and MLVSS$/$MLSS ratio of $\backslash (83\mathrm{.}3\backslash \%\backslash )$ are to be used. If the duration of each cycle is $6$ hours, for a threetank SBR system, determine appropriate dimensions $($length$,$ width, and depth$)$ of each tank.