Let the length be L, area A, the temperature of the sink T1, the temperature of the source T2 and the temperature of the junction T.
For the first conductor, the thermal rate is given by
H1t=KAT−T1L . . . . (1)
For the second conductor,
H2t=2KAT2−TL . . . . (2)
The two slabs are connected in series so the heat current flowing through them will be same. So,
KAT−T1L=2KAT2−TL
⇒(T−T1)=2(T2−T)
⇒T=13(2T2+T1) . . . . (3)
Let the equivalent coefficient of thermal conductivity be K'
Adding 1 and 2
H1+H2t=KAT−T1L+2KAT2−TL
⇒Ht=[KA{13(2T2+T1)−T1}+2KA{T2−13(2T2+T1)}]L
⇒Ht=KA43(T2−T1)L
⇒Ht=(43K)(T2−T1)L
⇒Ht=K′T2−T1L
So, equivalent thermal conductivity, K′=43K