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rodikova [14]
4 years ago
14

Lab scale tests performed on a cell broth with a viscosity of 5cP gave a specific cake resistance of 1 x 1011 cm/g and a negligi

ble medium resistance. The cake solids (dry basis) per volume of filtrate was 15 g/liter. It is desired to operate a larger rotary vacuum filter (diameter 8 m and length 12 m) at a vacuum pressure of 80 kPA with a cake formation time of 20 s and a cycle time of 60 s. Determine the filtration rate in volumes/hr expected for the rotary vacuum filter?
Engineering
1 answer:
navik [9.2K]4 years ago
6 0

Answer:

473,400 L/h

Explanation:  

For an incompressible cake and negligible medium resistance, we can find the  volume of filtrate collected using the following equation:

V_{f}^{2} = \frac{2A^{2}t_{f}\Delta P}{\mu \alpha \rho}     (1)          

<u>Where:</u>

V_{f}: is the volume of filtrate collected  

A: is the filtration area  

t_{f}: is the cake formation time = 20 s  

ΔP: is the vacuum pressure = 80 kPa  

μ: is the viscosity = 5 cP  

α: is the specific cake resistance = 1x10¹¹ cm/g  

ρ: is the cake solid per volume of filtrate = 15 g/L<em>  </em>   <em>     </em>

First, we need to convert the units:  

\mu = 5 cP \cdot \frac{0.01 g/cm*s}{1 cP} = 0.05 \frac{g}{cm*s}

\rho = 15 \frac{g}{L} \cdot \frac{1 L}{1000 cm^{3}} = 15 \cdot 10^{-3} g/cm^{3}      

\Delta P = 80\cdot 10^{3} Pa = 80\cdot 10^{3} \frac{N}{m^{2}} = 80 \cdot 10^{3} \frac{kg}{m*s^{2}} \cdot \frac{1000 g * 1 m}{1 kg * 100 cm} = 8.0 \cdot 10^{5} gcm^{-1}s^{-2}

Now, we need to find the filtration area (A), which is equal to a cylinder area:    

A = 2 \pi r^{2} + 2 \pi rh

<em>where r: is the radius = 8/2 m and h: is the height of the side = 12 m.    </em>

A = 2\pi (4m)^{2} + 2\pi 4m*12m = 4.02 \cdot 10^{6} cm^{2}  

Now, we can calculate the volume of filtrate using equation (1):    

V_{f} = \sqrt {\frac{2(4.02 \cdot 10^{6} cm^{2})^{2}*20 s*8 \cdot 10^{5} gcm^{-1}s^{-2}}{0.05 gcm^{-1}s^{-1}*1 \cdot 10^{11}cmg^{-1}*15 \cdot 10^{-3} gcm^{-3}}} = 2.63 \cdot 10^{6} cm^{3}

Finally, we can calculate the filtration rate in volumes/hr:  

rate = \frac{V_{f}}{t_{f}} = \frac{2.63 \cdot 10^{6} cm^{3}}{20 s} \cdot \frac{3600 s * 1 L}{1 h * 1000 cm^{3}} = 473,400 L/h      

 

I hope it helps you!      

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3 years ago
Air exits a compressor operating at steady-state, steady-flow conditions at 150 oC, 825 kPa, with a velocity of 10 m/s through a
ioda

Answer:

a) Qe = 0.01963 m^3 / s , mass flow rate m^ = 0.1334 kg/s

b) Inlet cross sectional area = Ai = 0.11217 m^2 , Qi = 0.11217 m^3 / s    

Explanation:

Given:-

- The compressor exit conditions are given as follows:

                  Pressure ( Pe ) = 825 KPa

                  Temperature ( Te ) = 150°C

                  Velocity ( Ve ) = 10 m/s

                  Diameter ( de ) = 5.0 cm

Solution:-

- Define inlet parameters:

                  Pressure = Pi = 100 KPa

                  Temperature = Ti = 20.0

                  Velocity = Vi = 1.0 m/s

                  Area = Ai

- From definition the volumetric flow rate at outlet ( Qe ) is determined by the following equation:

                   Qe = Ae*Ve

Where,

           Ae: The exit cross sectional area

                   Ae = π*de^2 / 4

Therefore,

                  Qe = Ve*π*de^2 / 4

                  Qe = 10*π*0.05^2 / 4

                  Qe = 0.01963 m^3 / s

 

- To determine the mass flow rate ( m^ ) through the compressor we need to determine the density of air at exit using exit conditions.

- We will assume air to be an ideal gas. Thus using the ideal gas state equation we have:

                   Pe / ρe = R*Te  

Where,

           Te: The absolute temperature at exit

           ρe: The density of air at exit

           R: the specific gas constant for air = 0.287 KJ /kg.K

             

                ρe = Pe / (R*Te)

                ρe = 825 / (0.287*( 273 + 150 ) )

                ρe = 6.79566 kg/m^3

- The mass flow rate ( m^ ) is given:

               m^ = ρe*Qe

                     = ( 6.79566 )*( 0.01963 )

                     = 0.1334 kg/s

- We will use the "continuity equation " for steady state flow inside the compressor i.e mass flow rate remains constant:

              m^ = ρe*Ae*Ve = ρi*Ai*Vi

- Density of air at inlet using inlet conditions. Again, using the ideal gas state equation:

               Pi / ρi = R*Ti  

Where,

           Ti: The absolute temperature at inlet

           ρi: The density of air at inlet

           R: the specific gas constant for air = 0.287 KJ /kg.K

             

                ρi = Pi / (R*Ti)

                ρi = 100 / (0.287*( 273 + 20 ) )

                ρi = 1.18918 kg/m^3

Using continuity expression:

               Ai = m^ / ρi*Vi

               Ai = 0.1334 / 1.18918*1

               Ai = 0.11217 m^2          

- From definition the volumetric flow rate at inlet ( Qi ) is determined by the following equation:

                   Qi = Ai*Vi

Where,

           Ai: The inlet cross sectional area

                  Qi = 0.11217*1

                  Qi = 0.11217 m^3 / s    

- The equations that will help us with required plots are:

Inlet cross section area ( Ai )

                Ai = m^ / ρi*Vi  

                Ai = 0.1334 / 1.18918*Vi

                Ai ( V ) = 0.11217 / Vi   .... Eq 1

Inlet flow rate ( Qi ):

                Qi = 0.11217 m^3 / s ... constant  Eq 2

               

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Will mark brainliest!
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<h2>i HOPE IT'S HELP </h2>
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3 years ago
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