(Solved): please help Draw for me the points on the PH diagram thankyou \begin{tabular}{|c|c|c|} \hline R134 P ...

\begin{tabular}{|c|c|c|} \hline R134 Pressire compressor suction. & $\mathrm{PI}[\mathrm{DCN}/\mathrm{m}]$ & 280 \\ \hline H13a Pressate at compressor delivery & $P2(\mathrm{NCN}/\mathrm{m}$ ? & 800 \\ \hline G1 Ma Terspersture at compressor suction & 710 & 15.1 \\ \hline Exida Temperature at compressor delivery & $12+9$ & \\ \hline B1 Wa lemperature at condenser outlet. & & 30 \\ \hline fl1 4 in femperature at expansion valve outlet & $\mathrm{is}\mathrm{kg}$ & \\ \hline linput power & C. chaty & 267 \\ \hline Water mass flow rite & move torlaed & 30 \\ \hline Water intet temperature & is $\mathrm{CE}$ & 10 \\ \hline Wateroutlet temperature & & \\ \hline Gisha mans liow rate. & |nir |ivicen| & 56 \\ \hline \end{tabular} \begin{tabular}{|c|c|c|} \hline & & input \\ \hline Absolute pressures & Pabs (Koa) & $3x$ \\ \hline CP: Specificheat capacity & $\mathrm{ka}/\mathrm{kec}$ & C.11 \\ \hline \multicolumn{3}{|c|}{ Condenser. } \\ \hline Heat transfer from refrigerant & (q cond) ret (w) & -garil \\ \hline Heat transfer to water & ta condf water $(w)$ & theoli \\ \hline \multicolumn{3}{|c|}{ Compressor } \\ \hline \begin{tabular}{l} Heat transfer to refrigerant calculated \\ by enthapy change of rasas \end{tabular} & W eomp (w) & 221 \\ \hline Heat loss from compresur & Qheur (w) & ais \\ \hline \end{tabular} \begin{tabular}{|c|c|c|} \hline Enthelpy at stage 1 & $\mathrm{h}1(\mathrm{Kj}/\mathrm{Kg})$ & 310 \\ \hline Enthelpy at stage 2 & $\mathrm{h}2(\mathrm{Kj}/\mathrm{Kg})$ & 350 \\ \hline Enthelpy at stage 3 & $\mathrm{h}3(\mathrm{Kj}/\mathrm{Kg})$ & 137 \\ \hline Enthelpy at stage 4 & $\mathrm{h}4(\mathrm{Kj}/\mathrm{Kg})$ & 137 \\ \hline \end{tabular} Table 3: Represent the enthelpy