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To prepare nuclear fuel, U3O8 ("yellow cake") is converted to UO2(NO3)2, which is then converted to UO3 and finally UO2.The fuel is enriched (the proportion of the 235U is increased) by a two-step conversion of UO2 into UF6, a volatile solid, followed by a gaseous-diffusion separation of the 235Uand238Uisotopes:

UO2(s)+4HF(g)UF4(s)+2H2O(g)UF4(s)+F2(g)UF6(s)

Calculate ΔG° for the overall process at 85°C.

Short Answer

Expert verified

At 85°C(358K),the overall processΔGrxn is equal to -370.497 kJ/mol.

Step by step solution

01

Concept Introduction

The reactions of the fuel enrichment process are first written down:

UO2(s)+4HF(g)UF4(s)+2H2O(g)UF4(s)+F2(g)UF6(s)

To calculate the Gibb's energy change for the process, we must keep in mind that the process occurs at 85°C(358K),therefore the conventional Gibb's energy values supplied are insufficient.

We may then compute Gibb's energy change for the process at the requisite temperature after calculating the enthalpy and entropy changes of the entire process.

02

Calculation for ΔXrxn° 

Let us calculate ΔXrxn°

Both enthalpy and entropy are state functions, which means they solely depend on the system's starting and ultimate states:

ΔHren°=ΔHproducts°-ΔHreactants°ΔSrxn°=ΔSproducts°-ΔSreactants°

The products in this example are all chemicals created by both reactions, and the reactants are also all compounds produced by both reactions.

If is a thermodynamic state function,

ΔXrxn°=[ΔX°(UF4(s))+2×ΔX°(H2O(g))+ΔX°(UF6(s))]-[ΔX°(UO2(s))+4×ΔX°(HF(g))+ΔX°(UF4(s))+ΔX°(F2(g))]

We can simplify that equation,

ΔXrxn°=[2×ΔX°(H2O(g))+ΔX°(UF6(s))]-[ΔX°(UO2(s))+4×ΔX°(HF(g))+ΔX°(F2(g))]

This is the simplified equation for

03

Calculating for Enthalpy and Entropy

Then, using Appendix B, for enthalpy we can write and calculate that,

ΔHrxn°=[2×ΔH°(H2O(g))+ΔH°(UF6(s))]-[ΔH°(UO2(s))+4×ΔH°(HF(g))+ΔH°(F2(g))]ΔHrxn°=(2mol×(-241.826kJmol)+1mol×(-2197.00kJmol))-(1mol×(-1085.00kJmol+4mol×(-273.00kJmol)+1mol×(0.00kJmol))ΔHrxn°=-503.652kJmol

Therefore, the enthalpy is -503.652kJmol

Similarly, for entropy we can write and calculate that,

ΔSrxn°=[2×ΔS°(H2O(g))+ΔS°(UF6(s))]-[ΔS°(UO2(s))+4×ΔS°(HF(g))+ΔS°(F2(g))]ΔSrxn°=(2mol×(188.72Jmol×K)+1mol×(225.00Jmol×K))-(1mol×(77.00Jmol×K+4mol×(173.67Jmol×K+1mol×(202.70Jmol×K)ΔSrxn°=-371.94Jmol×K

Thus, the entropy is,-371.94Jmol×K

04

Calculating Gibb’s Free Energy

Finally, Gibb's free energy change can be calculated at 85°C(358K)

ΔGrxn=ΔHrxn°-T×ΔSrxn°ΔGrxn=-503.652kJmol-358K×(-371.94Jmol×K)×10-3kJJΔGrxn=-370.497kJ

Therefore, at85°C(358K),ΔGrxn=-370.497kJ/mol

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Most popular questions from this chapter

Oxyacetylene welding is used to repair metal structures, including bridges, buildings, and even the Statue of Liberty. Calculate ΔSofor the combustion of1mole of acetyleneC2H2.

According to advertisements, "a diamond is forever."

(a) Calculate ΔH°,ΔS° , and ΔG° at 298k for the phase change Diamond graphite.

(b) Given the conditions under which diamond jewelry is normally kept, argue for and against the statement in the ad.

(c) Given the answers in part (a), what would need to be done to make synthetic diamonds from graphite?

(d) Assumingrole="math" localid="1663313565397" ΔH°androle="math" localid="1663313547943" ΔS°do not change with temperature, can graphite be converted to diamond spontaneously at 1 atm?

Find ΔSofor the reaction of nitrogen monoxide with hydrogen to form ammonia and water vapor. Is the sign ofrole="math" localid="1663358976150" ΔSoas expected?

Propylene (propene;CH3CH = CH2 ) is used to produce polypropylene and many other chemicals. Although most is obtained from the cracking of petroleum, about2% is produced by catalytic dehydrogenation of propane ( CH3CH2CH3):

CH3CH2CH3Pt/Al2O3CH3CH = CH2+H2

Because this reaction is endothermic, heaters are placed between the reactor vessels to maintain the required temperature.

(a) If the molar entropyS°, , of propylene is267.1 J/molK , find its entropy of formation, Sfo.

(b) Find Gf°of propylene (Hf°for propylene= 20.4 kJ/mol).

(c) Calculate Hrxn° andGrxn° for the dehydrogenation.

(d) What is the theoretical yield of propylene at 580°C if the initial pressure of propane is 1.00atm?

(e) Would the yield change if the reactor walls were permeable toH2 ? Explain.

(f) At what temperature is the dehydrogenation spontaneous, with all substances in the standard state?

Use Appendix B to determine the KspofAg2S.

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