Concept explainers
(a)
Interpretation:
The feed rates of the SO2 and air feed streams and the extent of reaction, e should be calculated.
Concept Introduction
The feed rates and extent of reactions can be better explained on the basis of flow chart formed from the given data.
(b)
Interpretation:
Calculate the standard heat of the SO2 oxidation reaction in kJ. Taking molecular species at 25? as references, an inlet-outlet enthalpy table should be prepared and filled in. Write an energy balance to calculate the necessary rate of heat transfer (kW) from the reactor to the cooling water.
Concept introduction:
The standard heat of formation will be helpful to solve the problem as:
(c)
Interpretation:
Calculate the minimum flow rate of heat transfer (kW) from the reactor to the cooling water.
(d)
Interpretation:
The result if element species is taken into calculation in part (b) should be stated.

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Chapter 9 Solutions
EBK ELEMENTARY PRINCIPLES OF CHEMICAL P
- Untuk sistem gas etilena (1)/propilena (2), estimasi (f^1, f^2, $^1, dan ^2 pada t = 150°C, P = 30 bar, dan y1 = 0,35; kij = 0. (a) Dengan menerapkan Persamaan (10.63). (b) Dengan asumsi bahwa campuran adalah lingkungan idealarrow_forwardOnly focus on H(3), which is the specific enthalpy for nitrogen gas. chemical engineeringarrow_forwardchemical engineering. Only focus on H(3), which is the nitrogen gas. Start with the reference state to the process state. Be thorough to the fullestarrow_forward
- acetone with these parameters: po:=101325; #Standard atmospheric pressure in PaTfo:=273.15-94.45; #Melting temperature in K Tvo:=273.15+56.15; #Boiling temperature in K Hv:=31270; #Enthalpy of vaporization in J/molR:=8.314; #Gas Constant in J/mol*KNLe:=1.76; #Lewis number for acetoneMw:= 0.05808 ; #kg/mol molecular weight of acetoneW0:= 0.15; Wsp:=0.005;Am:= 0.12; #m^2/kg dry solid for the exposed wet areah:= 11; #W/m^2K for heat transfer coefficienttau__min:= Hv*(W0-Wsp)/Mw/Am/h/(T8-TS); tau__min/60;arrow_forwardchemical engineering Material-energy balance. Only focus on the nitrogen gas, which is H(3)arrow_forward1. The settling chamber, shown schematically in Figure 2E1.1, is used as a primary separation device in the removal of dust particles of density 1500 kg/m³ from a gas of density 0:7 kg/m³ and viscosity 1.90 x 10-5 Pa s. Gas inlet Elevation Gas Gas exit exit H Collection surface -W Section X-X Dimensions: H=3m L = 10 m W=2m Figure 2E1.1 Schematic diagram of settling chamber Assuming Stokes' law applies, show that the efficiency of collection of particles of size x is given by the expression collection efficiency, x = x²8(pp - Pi)L 18μHU where U is the uniform gas velocity through the parallel-sided section of the chamber. State any other assumptions made. (b) What is the upper limit of particle size for which Stokes' law applies? (c) When the volumetric flow rate of gas is 0.9 m³/s, and the dimensions of the chamber are those shown in Figure 2E1.1, determine the collection efficiency for spherical particles of diameter 30 mm.arrow_forward
- Can you answer this sequantially correct like show me the full process. Also, since it is chemical engineering related problem a perry's handbook is used. Thank youarrow_forwardchemical engineering Demonstrate how each specific enthalpy was calculated, from the reference state to the process state. Be thorough to the fullest. This is a material-energy balance. The answers are H(1) = 35.7 KJ/kmol, H(2) = 32.0 KJ/kmol, and H(3) = -1.26 KJ/kmol.arrow_forwardheat and mass transfer:arrow_forward
- Chemical Engineering. Be thorough to the fullest for the three enthalpies. H(1) = 35.7 kj/kmol H(2) =32.0 Kj/kmol H(3)= -1.26 Kj/kmolarrow_forwardchemical engineering Only solve the specific enthalpies. Be thorough to the fullest for each calculationarrow_forwardDo question 9 please! Question 7 Is just there for reference!!arrow_forward
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