Problem 5.6a Ammonia Process - Energy Balance for Mixer into R2 Using average molar heat capacities 7.427.02Tref (K) 273.15 11.8614.57S 3 4.97323.15 Temp (K) Feed2507.98 N(N2) Feed7522.93 N(H2) Feed 708.06 Temp (K) R1 out0.00 N(NH3) Feed 4213.73 N(N2) R1 out96.54 N(CH4) Feed 10900.89 N(H2) R1 out34.55 N(Ar) Feed 1962.67 N(NH3) R1 out3649923.65 Feed 2153.99 N(CH4) R1 out460.52 N(Ar) R1 out Use Goal See to !ar" T R2 #$%%% R1 out &$er'" (ala$)e * 0 (out + ,$)50% of Feed S 2 0S 3a MixerS 4638.25 Temp (K) R2 #$ 689.18 Temp (-)5467.72 N(N2) R2 #$14662.35 N(H2) R2 #$1962.67 N(NH3) R2 #$2202.26 N(CH4) R2 #$477.80 N(Ar) R2 #$%%% R2 #$.p/2.p02.p/03.p.04.p1rNshs (C!)Nshs (C!)Nshs (C!)