When two streams of the same fluid mix adiabatically in a steady flow with no work done, energy conservation means the total enthalpy carried in by both streams must equal the enthalpy carried out by the combined stream. There is no heat loss to account for since both tubes are insulated.
For an ideal gas with constant $C_p$, the enthalpy flow of a stream is just $\dot{m} C_p T$. Writing the balance for the two inlet streams and the single outlet stream gives $\dot{m}_1 C_p T_1 + \dot{m}_2 C_p T_2 = (\dot{m}_1 + \dot{m}_2) C_p T_{mix}$, and since $C_p$ appears in every term it drops out completely.
What remains is a mass flow weighted average of temperature. Plugging in $\dot{m}_1 = 0.1$ kg/s at $20$ C and $\dot{m}_2 = 0.2$ kg/s at $25$ C gives $T_{mix} = (0.1 \times 20 + 0.2 \times 25)/(0.1+0.2) = 7/0.3$.
Working that out gives $T_{mix} = 23.33$ C, which rounds to $23.3$ C, the steady state temperature of the combined air stream.