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Solutions Manual For Ballistics Theory and Design of Guns and Ammunition 3rd Edition By Donald E. Carlucci; Sidney S. Jacobson ISBN:9781138055315 ALL Chapters Covered||COMPLETE GUIDE A+||.

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Solutions Manual For Ballistics Theory and Design of Guns and Ammunition 3rd Edition By Donald E. Carlucci; Sidney S. Jacobson ISBN:9781138055315 ALL Chapters Covered||COMPLETE GUIDE A+||.

Institución
Ballistics 3rd Edition
Grado
Ballistics 3rd Edition











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Institución
Ballistics 3rd Edition
Grado
Ballistics 3rd Edition

Información del documento

Subido en
3 de mayo de 2025
Número de páginas
928
Escrito en
2024/2025
Tipo
Examen
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Ballistics: The Theory and Design
@SW @SW @SW @SW




of Ammunition and Guns 3rd
@SW @SW @SW @SW @SW




Edition @SW




Solutions Manual Part 0 @SW @SW @SW




Donald E. @SW




Carlucci Sidney
@SW @SW




@SWS. Jacobson
@SW




** Immediate Download
@SW @SW




** Swift Response
@SW @SW




** All Chapters included
@SW @SW @SW



2.1 The Ideal Gas Law
Problem 1 - Assume we have a quantity of 10 grams of 11.1% nitrated nitrocellulose
(C6H8N2O9) and it is heated to a temperature of 1000K and changes to gas somehow
without changing chemical composition. If the process takes place in an expulsion cup
with a volume of 10 in3, assuming ideal gas behavior, what will the final pressure be in
psi?
 lbf 
Answer p = 292
in 2 

Solution:

,This problem is fairly straight-forward except for the units. We shall write our ideal gas
law and let the units fall out directly. The easiest form to start with is equation (IG-4)

pV = mg RT (IG-4)

Rearranging, we have

mg RT
p=
V

Here we go  
   
(10)g 1  kg (8.314) kJ  1  kgmol (737.6)ft − lbf (12)in (1000)K
1000 g kgmol  K     
     252   CHNO
kg  kJ  ft 
2 9 
p= 
 
6

(10) in 3
8




 lbf 
p = 292
in 2 

You will notice that the units are all screwy – but that’s half the battle when working
these problems! Please note that this result is unlikely to happen. If the chemical
composition were reacted we would have to balance the reaction equation and would
have to use Dalton’s law for the partial pressures of the gases as follows. First, assuming
no air in the vessel we write the decomposition reaction.

C6 H8 N 2 O9 → 4H 2 O + 5CO + N 2 + C(s)

Then for each constituent (we ignore solid carbon) we have

, NiT
pi =
V

So we can write   kJ  kgmolC6 H8 N 2O9 
(4) kgmol H O (8.314)
 
(1000)K 1  (10) gC6 H8 N 2O9 
 1 kg C H N O
   6 8 2 9


kgmolC H N O  kgmol - K    1,000  g C H N O 
   C H N O
p = 6 8 2 9 
2
252  kg 6 8 2 9   6 8 2 9 
H 2O ( ) 3  1  kJ  1  ft   
10 in     
 737.6 ft − lbf  12 in 
lbf 
= 1,168
pH2O in 2 
    1 kgmolC6 H8 N2O9 
(1000)K (10)g
kJ
(5) kgmolCO (8.314)  1 kg C6 H8 N2O9 
       





  C H NO
kgmol kgmol - K 252 kg 6 8 2 9
1,000 g
 C H N O         C H N O 

C H N O
CO

p = ( )  
6 8 2 9  3
6 18 29ft   6 8 2 9 
10 in  

1  kJ
pCO  lbf 
= 1,460  737.6 ft − lbf  12 in 
 in 2   
  1 kgmol 1 kg C6 H8 N2O9 
(1)   
kgmol (8.314) kJ
(1000)K C6 H8 N2O9
(10)g 
 
N2
       
C6 H8 N2O9
kgmol kgmol - K 252 kg 1,000 g


( )
N2

 C H N O      C H N O    C H N O 
p = 




6 8 2 9   1  kJ   6 8 2 9   6 8 2 9 
lbf  10 in 3  1  ft 
pN = 292  737.6  ft − lbf  12 in 
in 2 
2




2 2



Then the total pressure is
p = pH O +lbpfCO+ pN  lbf  lbf  lbf 
p = 1,168 in 2  + 1,460 + 292 = 2,920
in 2  in 2  in 2 
2.2 Other Gas Laws
Problem 2 - Perform the same calculation as in problem 1 but use the Noble-Abel
equation of state and assume the covolume to be 32.0 in3/lbm

,  lbf 
Answer: p = 314.2
in 2 

Solution:

This problem is again straight-forward except for those pesky units – but we’ve done this
before. We start with equation (VW-2)

p(V − cb) = mg RT (VW-2)

Rearranging, we have

mg RT
p=
V − cb

Here we go  
   
(10)g 1  kg (8.314) kJ  1  kgmol (737.6)ft − lbf (12)in (1000)K
1000 g kgmol  K     
     252 kg C H N O   kJ  ft 
p=   6 8 2 9 

 
(10) in 3 − (10 )g 1000
 1  kg(2.2 )lbm (32.0 ) in3 
g kg  lbm 
      

 lbf 
p = 314.2
in 2 

So you can see that the real gas behavior is somewhat different than ideal gas behavior at
this low pressure – it makes more of a difference at the greater pressures.

Again please note that this result is unlikely to happen. If the chemical composition were
reacted we would have to balance the reaction equation and would again have to use
Dalton’s law for the partial pressures of the gases. Again, assuming no air in the vessel
we write the decomposition reaction.

C6 H8 N 2 O9 → 4H 2 O + 5CO + N 2 + C(s)

Then for each constituent (again ignoring solid carbon) we have

Ni T
pi =
(V - cb)
So we can write
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