Please give full solution with each step. Values can be found in the table provided. Will upvote

3. ( 9 marks total) The cylinder of a refrigeration compressor initially contains 0.1L of saturated vapour R134a at 20C. The R134a is then compressed in a polytropic process (PVn, with n=1.1) to a final pressure of 1MPa. (a) (4 marks) Determine the final temperature T2. (b) (4 marks) Calculate the total work and the heat transfer in kJ. (b) (1 mark) Sketch this process on a P-v diagram, showing its relation to the saturation region. Tables for Refrigerant R134a Properties of superheated R134a \begin{tabular}{|c|c|c|c|c|c|c|c|c|c|} \hline \multirow[b]{2}{*}{T(C)} & \multicolumn{3}{|c|}{100kPa(26.5C)} & \multicolumn{3}{|c|}{300kPa(0.56C)} & \multicolumn{3}{|c|}{1000kPa(39.37C)} \\ \hline & \begin{tabular}{l} v \\ (m3/kg) \end{tabular} & \begin{tabular}{l} u \\ (kJ/kg) \end{tabular} & \begin{tabular}{l} s(kJ/kg \\ K) \end{tabular} & \begin{tabular}{l} v \\ (m3/kg) \end{tabular} & \begin{tabular}{l} u \\ (kJ/kg) \end{tabular} & \begin{tabular}{l} s(kJ/kg \\ K) \end{tabular} & v(m3/kg) & \begin{tabular}{l} u \\ (kJ/kg) \end{tabular} & s(kJ/kgK) \\ \hline sat. & 0.19257 & 362.73 & 1.7456 & 0.06787 & 378.33 & 1.7259 & 0.02038 & 399.16 & 1.7125 \\ \hline-20 & 0.19860 & 367.36 & 1.7665 & & & & & & \\ \hline-10 & 0.20765 & 374.51 & 1.7978 & & & & & & \\ \hline 0 & 0.21652 & 381.76 & 1.8281 & & & & & & \\ \hline 10 & 0.22527 & 389.14 & 1.8578 & 0.07111 & 385.84 & 1.7564 & & & \\ \hline 20 & 0.23392 & 396.66 & 1.8869 & 0.07441 & 393.80 & 1.7874 & & & \\ \hline 30 & 0.24250 & 404.31 & 1.9155 & 0.07762 & 401.81 & 1.8175 & & & \\ \hline 40 & 0.25101 & 412.12 & 1.9436 & 0.08075 & 409.90 & 1.8468 & 0.02047 & 399.78 & 1.7148 \\ \hline 50 & 0.25948 & 420.08 & 1.9712 & 0.08382 & 418.09 & 1.8755 & 0.02185 & 409.39 & 1.7494 \\ \hline 60 & 0.26791 & 428.20 & 1.9985 & 0.08684 & 426.39 & 1.9035 & 0.02311 & 418.78 & 1.7818 \\ \hline 70 & 0.27631 & 436.47 & 2.0255 & 0.08982 & 434.82 & 1.9311 & 0.02429 & 428.05 & 1.8127 \\ \hline 80 & 0.28468 & 444.89 & 2.0521 & 0.09277 & 443.37 & 1.9582 & 0.02542 & 437.29 & 1.8425 \\ \hline 90 & 0.29302 & 453.47 & 2.0784 & 0.09570 & 452.07 & 1.9850 & 0.02650 & 446.53 & 1.8713 \\ \hline 100 & 0.30135 & 462.21 & 2.1044 & 0.09861 & 460.90 & 2.0113 & 0.02754 & 455.82 & 1.8994 \\ \hline \end{tabular}