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kompoz [17]
3 years ago
10

(a) For BCC iron, calculate the diameter of the minimum space available in an octahedral site at the center of the (010) plane,

and compare this to the diameter of a carbon atom. Assume that the iron atoms in the BCC structure are hard spheres that touch along the [111] direction.
(b) Compare the space available with the size of a carbon atom from Appendix C, and comment about the potential solubility of carbon in BCC iron in octahedral interstitial sites.
Engineering
1 answer:
Romashka-Z-Leto [24]3 years ago
7 0

Answer:

a) diameter available = 0.0384 nm

b)The space  is smaller than the carbon atom which has a  radius of  0.077 nm and this simply means that the carbon atom will not conquer these sites

Explanation:

For BCC iron

From Appendix B given,select the lattice parameter ( a ) as = 0.2866 nm

The BCC iron has 4 atomic radii and therefore the body diagonal length = a(3)^\frac{1}{2}

expressing the atomic radius of the BCC iron

4r = a(3)^\frac{1}{2}

insert the value of (a) from appendix B which is = 0.2866 nm

4r = 0.2866 nm (3)^\frac{1}{2}

therefore  r =  0.4964 nm / 4 = 0.1241 nm

Refer again to appendix C given select the atomic radius of the BCC iron as = 0.1241 nm   assuming the atomic radius of the iron are the same

then the radius ratio = 0.62

Refer to the Figure 3.2 given, the amount of space required for an interstitial at the BCC position is between the atoms at the FCC position and also in this space there are two atoms that are equal to a radius of 0.2482 nm

The diameter of the minimum space available

d_{a} = a - r_{a}

r_{a}  = atomic radii = 0.2482 nm

a = 0.2666 nm

therefore

d_{a} = 0.2866 nm - 0.2482 nm = 0.0384 nm

comparing this to the diameter of a carbon atom

The space  is smaller than the carbon atom which has a  radius of  0.077 nm and this simply means that the carbon atom will not conquer these sites

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\\ E_{inflow} = E_{outflow}

Note: from the question we have only one source of inflow and two source of outflow (the exhaust at a pressure of 50kpa and the feedwater at a pressure of 5ookpa). Also the power produce is another source of outgoing energy    \\ E_{inflow} = m_{1} h_{1} .

\\

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\\

Where m_{1} h_{1} are the mass flow rate and the enthalpies at the inlet  at a pressure of 3Mpa \\,

m_{2} h_{2} are the mass flow rate and the enthalpies  at the outlet 2 where we have a pressure of 500kpa respectively.\\,

and  m_{3} h_{3}   are the mass flow rate and the enthalpies  at the outlet 3 where we have a pressure of 50kpa respectively.\\,

We can now express write out the required equation by substituting the new expression for the energies \\

m_{1} h_{1} = m_{2} h_{2} + m_{3} h_{3} + W_{out}   \\

from the above equation, the unknown are the enthalpy values and  the mass flow rate. \\

first let us determine the enthalpy values at the inlet and the out let using the Superheated water table.  \\

It is more convenient to start from outlet 3 were we have a temperature 100^{0}C and pressure value of (50kpa or 0.05Mpa ). using double interpolation method  on the superheated water table to determine the enthalpy value with careful calculation we have  \\

h_{3}  = 2682.4 KJ/KG , at this point also from the table the entropy value ,s_{3} value is 7.6953 KJ/Kg.K. \\

Next we determine the enthalphy value at outlet 2. But in this case, we don't have a temperature value, hence we use the entrophy value since the entropy  is constant at all inlet and outlet. \\

So, from the superheated water table again, at a pressure of 500kpa (0.5Mpa) and entropy value of  7.6953 KJ/Kg.K with careful  interpolation we arrive at a enthalpy value of 3206.5KJ/Kg.\\

Finally for inlet one at a pressure of 3Mpa, interpolting with an entropy value of 7.6953KJ/Kg.K  we arrive at enthalpy value of 3851.2KJ/Kg. \\

Now we determine the mass flow rate at each inlet and outlet. since  mass must also be balance, i.e  m_{1} = m_{2} + m_{3} \\

From the question the, the mass flow rate at the inlet m_{1}}  is 2Kg/s \\

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m_{3} = 0.95m_{1} = 0.95 *2kg/s = 1.9kg/s \\

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\\

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