A liquid food with 12% total solids is being heated by steam injection using steam at a pressure of 232.1 kPa (Fig. E3.3). The product enters the heating system at 508C at a rate of 100 kg/min and is being heated to 1208C. The product specific heat is a function of composition as follows: cp 5 cpwðmass fraction H2OÞ 1 cpsðmass fraction solidÞ and the specific heat of product at 12% total solids is 3.936 kJ/(kg 8C). Determine the quantity and minimum quality of steam to ensure that the product leaving the heating system has 10% total solids.

Respuesta :

Answer:

[tex]m_{s}=20kg/min[/tex]

[tex]H_{s}=1914kJ/kg[/tex]

Explanation:

A liquid food with 12% total solids is being heated by steam injection using steam at a pressure of 232.1 kPa (Fig. E3.3). The product enters the heating system at 50°C at a rate of 100 kg/min and is being heated to 120°C. The product specific heat is a function of composition as follows:

[tex]c_{p}=c_{pw}(mass fraction H_{2}0)+c_{ps}(mass fraction solid)[/tex] and the

specific heat of product at 12% total solids is 3.936 kJ/(kg°C). Determine the quantity and minimum quality of steam to ensure that the product leaving the heating system has 10% total solids.

Given

Product total solids in ([tex]X_{A}[/tex]) = 0.12

Product mass flow rate ([tex]m_{A}[/tex]) = 100 kg/min

Product total solids out ([tex]X_{B}[/tex]) = 0.1

Product temperature in ([tex]T_{A}[/tex]) = 50°C

Product temperature out ([tex]T_{B}[/tex]) = 120°C

Steam pressure = 232.1 kPa at ([tex]T_{S}[/tex]) = 125°C

Product specific heat in ([tex]C_{PA}[/tex]) = 3.936 kJ/(kg°C)

The mass equation is:

[tex]m_{A}X_{A}=m_{B}X_{B}[/tex]

[tex]100(0.12)=m_{B}(0.1)\\m_{B}=\frac{100(0.12)}{0.1} =120[/tex]

Also [tex]m_{a}+m_{s}=m_{b}\\[/tex]

Therefore: [tex]100}+m_{s}=120\\\\m_{s}=120-100=20[/tex]

The energy balance equation is:

[tex]m_{A}C_{PA}(T_{A}-0)+m_{s}H_{s}=m_{B}C_{PB}(T_{B}-0)[/tex]

[tex]3.936 = (4.178)(0.88) +C_{PS}(0.12)\\C_{PS}=\frac{3.936-3.677}{0.12} =2.161[/tex]

[tex]C_{PB}= 4.232*0.9+0.1C_{PS}= 4.232*0.9+0.1*2.161=4.025[/tex]  kJ/(kg°C)

Substituting values in the energy equation:

[tex]100(3.936)(50-0)+20H_{s}=120(4.025)}(120-0)[/tex]

[tex]19680+20H_{s}=57960\\20H_{s}=57960-19680 \\20H_{s}=38280\\H_{s}=\frac{38280}{20} =1914[/tex]

[tex]H_{s}=1914kJ/kg[/tex]

From properties of saturated steam at 232.1 kPa,

[tex]H_{c}[/tex] = 524.99 kJ/kg

[tex]H_{v}[/tex] = 2713.5 kJ/kg

% quality = [tex]\frac{1914-524.99}{2713.5-524.99} =63.5%[/tex]

Any steam quality above 63.5% will result in higher total solids in

heated product

Lanuel

The quantity and minimum quality of steam are 20 Kg/min and 63.5 percent.

Given the following data:

  • Total solid = 12% = 0.12
  • Pressure = 232.1 kPa.
  • Steam temperature = 125°C
  • In temperature = 50°C
  • Out temperature = 120°C
  • Specific heat of product = 3.936 kJ/(kg°C).

How to calculate the quantity of product.

In order to determine the quantity of product, we would apply the mass balance equation and it is given as follows:

[tex]M_aX_a=M_bX_b[/tex]   ...equation 1.

[tex]M_a+M_s=M_b[/tex]    ...equation 2.

Where:

  • [tex]M_a[/tex] is the mass flow rate.
  • [tex]X_a[/tex] is the total solid in.
  • [tex]M_s[/tex] is the mass of solid.
  • [tex]M_b[/tex] is the mass of balance.
  • [tex]X_a[/tex] is the total solid out.

Substituting the given parameters into eqn. 1, we have;

[tex]100 \times 0.12=M_b \times 0.1\\\\12=0.1M_b\\\\M_b=\frac{12}{0.1} \\\\M_b=120 \; Kg/min[/tex]

From eqn. 2, we have:

[tex]M_a+M_s=M_b\\\\100+M_s=120\\\\M_s=120-100\\\\M_s =20 \; Kg/min[/tex]

Next, we would determine the enthalpy of steam ([tex]H_s[/tex]) by setting up an energy balance equation while using a reference temperature of 0°C:

[tex]M_aC_{pa}(T_a-0)+M_sH_s=M_bC_{pb}(T_b-0)[/tex]

For the specific heat of solid:

[tex]C_{ps}=\frac{[3.396-(4.178\times 0.88)]}{0.12} \\\\C_{ps}=2.161\;\;kJ/(kg^{\circ}C).[/tex]

For the specific heat of balance:

[tex]C_{pb}=C_{ps}(0.1)+4.232(0.9)\\\\C_{pb}=2.161(0.1)+3.8088\\\\C_{pb}=4.025\;kJ/(kg^{\circ}C).[/tex]

Substituting the parameters into the energy balance equation, we have:

[tex](100)(3.396)(50-0)+20H_s=120(4.025)(120-0)\\\\20H_s=120(4.025)(120)-(100)(3.396)(50)\\\\20H_s=57960-19680\\\\20H_s=38280\\\\H_s=\frac{38280}{20} \\\\H_s=1914\;kJ/kg[/tex]

From the steam table, the properties of saturated steam at 232.1 kPa are:

  • [tex]H_v=2713.5\; kJ/kg[/tex]
  • [tex]H_c=524.99\; kJ/kg[/tex]

For the steam quality, we have:

[tex]Q=\frac{H_s \;-H_c}{H_v \;-H_c} \\\\Q=\frac{1914 \;-\;524.99}{2713.5 \;-\;524.99} \\\\Q=\frac{1389.01}{2188.51}[/tex]

Q = 63.5%.

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