P2-3 FAo/-rA 10 8 4 0.2 0.4 0.6 0.8 1 0.1 0.2 0.4 0.6 0.7 0.8 FAo/-rA (m) 0.89 1.08 1.33 2.05 3.54 5.06 8.0 6. 2.

P2-3<br>FAo/-rA<br>10<br>8<br>4<br>0.2<br>0.4<br>0.6<br>0.8<br>1<br>0.1<br>0.2<br>0.4<br>0.6<br>0.7<br>0.8<br>FAo/-rA (m) 0.89<br>1.08<br>1.33<br>2.05<br>3.54<br>5.06 8.0<br>6.<br>2.<br>

Extracted text: P2-3 FAo/-rA 10 8 4 0.2 0.4 0.6 0.8 1 0.1 0.2 0.4 0.6 0.7 0.8 FAo/-rA (m) 0.89 1.08 1.33 2.05 3.54 5.06 8.0 6. 2.
Problems P2-3B You have two CSTRS and two PFRS, each with a volume of 1.6 m³. Use Figure 2-2B on page 43 to cal- culate the conversion for each of the reactors in the following arrangements. (a) Two CSTRS in series. (Ans.: X¡ = 0.435, X2 = 0.66) (b) Two PFRS in series. %3D %3D

Problems<br>P2-3B<br>You have two CSTRS and two PFRS, each with a volume of 1.6 m³. Use Figure 2-2B on page 43 to cal-<br>culate the conversion for each of the reactors in the following arrangements.<br>(a) Two CSTRS in series. (Ans.: X¡ = 0.435, X2 = 0.66)<br>(b) Two PFRS in series.<br>%3D<br>%3D<br>

Extracted text: Problems P2-3B You have two CSTRS and two PFRS, each with a volume of 1.6 m³. Use Figure 2-2B on page 43 to cal- culate the conversion for each of the reactors in the following arrangements. (a) Two CSTRS in series. (Ans.: X¡ = 0.435, X2 = 0.66) (b) Two PFRS in series. %3D %3D

Jun 08, 2022

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P2-3 FAo/-rA 10 8 4 0.2 0.4 0.6 0.8 1 0.1 0.2 0.4 0.6 0.7 0.8 FAo/-rA (m) 0.89 1.08 1.33 2.05 3.54 5.06 8.0 6. 2.

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