According to the reaction given below, product $D$ is produced in a chemical process. In the process whose flow diagram is given below, there is no B in the reactor exit stream.

$A+BC+D$

The fixed capital investment of the process is $$12106($ $$7106$ at the end of the first year and $$5106$ at the end of the second year$).$ The sources and amounts of cash flows after commissioning $($at the end of the $2$ nd year$)$ are given in the table below. Once put into operation, the life of the process is $10$ years. There is no waste processing cost.

$\begin{array}{cc}\text{C}\text{a}\text{s}\text{h}\text{F}\text{l}\text{o}\text{w}\text{S}\text{o}\text{u}\text{r}\text{c}\text{e}& \text{C}\text{a}\text{s}\text{h}\text{F}\text{l}\text{o}\text{w}(105\text{\$}\text{y}\text{e}\text{a}\text{r})\\ \text{P}\text{r}\text{o}\text{d}\text{u}\text{c}\text{t}\text{s}\text{a}\text{l}\text{e}\text{s}\text{r}\text{e}\text{v}\text{e}\text{n}\text{u}\text{e}& 20\mathrm{.}00\\ \text{R}\text{a}\text{w}\text{m}\text{a}\text{t}\text{e}\text{r}\text{i}\text{a}\text{l}\text{s}cost& 10\mathrm{.}70\\ \text{S}\text{e}\text{r}\text{v}\text{i}\text{c}\text{e}cost& 9\mathrm{.}00\\ \text{L}\text{a}\text{b}\text{o}\text{r}cost& 4\mathrm{.}50\end{array}$

As a result of the research, it was calculated that product C could be produced with $99\%$ purity instead of $92\mathrm{.}5\%$ by using an additional distillation column. In this way, while service costs will increase by $15\%,$ sales revenues are expected to increase by $30\%.$ There is no change in labor costs. The diameter of the distillation column that is planned to be added is $2\mathrm{.}5m$ and its height is $25m.$ There are $25$ trays in the column, and it is operated at $15$ barg, Columns and trays are made of stainless steel. The total cost of columns and trays accounts for $60\%$ of the total module cost of the new distillation system. Calculate the undepreciated production cost of the new $($modified$)$ process. $($CEPCI$2018=616\mathrm{.}0$; CEPCI$2001=397\mathrm{.}0).$