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Ad libitum [116K]
3 years ago
7

A reciprocating single-acting pump has a cylinder of 125mm bore and 300mm stroke and draws water from a sump whose water level i

s 1m below the axis of the pump. The suction pipe is 2 m long and has a diameter of 50mm. Calculate the speed in RPM at which separation occurs, if this takes place when the absolute pressure in the cylinder falls to 2.4m of water. Atmospheric pressure is equivalent to 10.3m of water. Assume simple harmonic motion of the piston. What is the maximum theoretical discharge in litres/min of this pump?
Engineering
1 answer:
djverab [1.8K]3 years ago
5 0

Answer:

speed is 57.38 rpm

theoretical discharge =3.54 litres /min

Explanation:

given data

bore r = 125 mm

stock = 300 mm

water level = 1m

pipe L = 2 m

diameter = 50 mm

absolute pressure = 2.4 m

atmospheric pressure = 10.3 m

to find out

theoretical discharge and speed

solution

we will apply here pressure formula here

pressure (s) =  L/g × ( Area (p) / Area(s) ) × ω²×r×cos∅

for maximum pressure ∅ = 0

so put here all value

pressure (s) =  2/9.8 × ( π/4×125² / π/4×50² ) × ω²×300/2

pressure (s) = 0.191 ω²

and we know

atmospheric pressure = absolute pressure + pressure (s) + water level

10.3 = 2.4 + 1 + 0.191 ω²

solve it and we get

ω = 6 rad/sec

so discharge = A× L× N /60

so here N = 57.38

speed is 57.38 rpm

and

theoretical discharge = A(p) L N / 60

theoretical discharge = π/4×125² × 2 × 57.38 / 60

theoretical discharge =3.54 litres /min

You might be interested in
Compressed Air In a piston-cylinder device, 10 gr of air is compressed isentropically. The air is initially at 27 °C and 110 kPa
Helen [10]

Answer:

(a) 2.39 MPa (b) 3.03 kJ (c) 3.035 kJ

Explanation:

Solution

Recall that:

A 10 gr of air is compressed isentropically

The initial air is at = 27 °C, 110 kPa

After compression air is at = a450 °C

For air,  R=287 J/kg.K

cv = 716.5 J/kg.K

y = 1.4

Now,

(a) W efind the pressure on [MPa]

Thus,

T₂/T₁ = (p₂/p₁)^r-1/r

=(450 + 273)/27 + 273) =

=(p₂/110) ^0.4/1.4

p₂ becomes  2390.3 kPa

So, p₂ = 2.39 MPa

(b) For the increase in total internal energy, is given below:

ΔU = mCv (T₂ - T₁)

=(10/100) (716.5) (450 -27)

ΔU =3030 J

ΔU =3.03 kJ

(c) The next step is to find the total work needed in kJ

ΔW = mR ( (T₂ - T₁) / k- 1

(10/100) (287) (450 -27)/1.4 -1

ΔW = 3035 J

Hence, the total work required is = 3.035 kJ

4 0
3 years ago
Which of these is not a type of socket
kotegsom [21]
You didn’t put a picture
7 0
3 years ago
The time to half-maximum voltage is how long it takes the capacitor to charge halfway. Based on your experimental results, how l
satela [25.4K]

Answer:

Time taken for the capacitor to charge to 0.75 of its maximum capacity = 2 × (Time take for the capacitor to charge to half of its capacity)

Explanation:

The charging of a capacitor/the build up of its voltage follows an exponential progression and is given by

V(t) = V₀ [1 - e⁻ᵏᵗ]

where k = (1/time constant)

when V(t) = V₀/2

(1/2) = 1 - e⁻ᵏᵗ

e⁻ᵏᵗ = 0.5

In e⁻ᵏᵗ = In 0.5 = - 0.693

-kt = - 0.693

kt = 0.693

t = (0.693/k)

Recall that k = (1/time constant)

Time to charge to half of max voltage = T(1/2)

T(1/2) = 0.693 (Time constant)

when V(t) = 0.75

0.75 = 1 - e⁻ᵏᵗ

e⁻ᵏᵗ = 0.25

In e⁻ᵏᵗ = In 0.25 = -1.386

-kt = - 1.386

kt = 1.386

t = 1.386(time constant) = 2 × 0.693(time constant)

Recall, T(1/2) = 0.693 (Time constant)

t = 2 × T(1/2)

Hope this Helps!!!

3 0
3 years ago
Read 2 more answers
Air flows through a rectangular section Venturi channel . The width of the channel is 0.06 m; The height at the inlet (1) and ou
nataly862011 [7]

Answer:

a) Q = 1.3044 m^3 / s

b) h2 = 0.37 m

c) Pi = Pe = Patm = 101.325 KPa

Explanation:

Given:-

- The constant width of the rectangular channel, b = 0.06 m

- The density of air, ρa = 1.23 kg/m^3

- The density of water, ρw = 1000 kg / m^3

- The height of the channel at inlet and exit, hi = he = 0.04 m

- The height of the channel at point 2 = h2

- The height of the channel at point 3 - Throat , ht = 0.02 m

- The change height of the water in barometer at throat, ΔHt = 0.1 m

- The change height of the water in barometer at point 2, ΔH2 = 0.05 m  

- The flow rate = Q

Solution:-

- The flow rate ( Q ) of air through the venturi remains constant because the air is assumed to be incompressible i.e ( constant density ). We have steady state conditions for the flow of air.

- So from continuity equation of mass flow rate of air we have:

                         m ( flow ) = ρa*An*Vn = Constant

Where,

             Ai : The area of the channel at nth point

             Vi : The velocity of air at nth point.

- Since, the density of air remains constant throughout then we can say that flow rate ( Q ) remains constant as per continuity equation:

                        Q = m ( flow ) / ρa

Hence,

                        Q = Ai*Vi = A2*V2 = At*Vt = Ae*Ve

- We know that free jet conditions apply at the exit i.e the exit air is exposed to atmospheric pressure P_atm.

- We will apply the bernoulli's principle between the points of throat and exit.

Assuming no changes in elevation between two points and the effect of friction forces on the fluid ( air ) are negligible.

                       Pt + 0.5*ρa*Vt^2 = Pe + 0.5*ρa*Ve^2

- To determine the gauge pressure at the throat area ( Pt ) we can make use of the barometer principle.

- There is an atmospheric pressure acting on the water contained in the barometric tube ( throat area ). We see there is a rise of water by ( ΔHt ).

- The rise in water occurs due to the pressure difference i.e the pressure inside the tube ( Pt ) and the pressure acting on the water free surface i.e ( Patm ).

- The change in static pressure leads to a change in head of the fluid.

Therefore from Barometer principle, we have:

              Patm - Pt-abs = pw*g*ΔHt

              101,325 - Pt-abs = 1000*9.81*0.1

              Pt-abs = 101,325 - 981

              Pt-abs = 100,344 Pa ..... Absolute pressure

- We will convert the absolute pressure into gauge pressure by the following relation:

             Pt = Pt-abs - Patm

             Pt = 100,344 - 101,325

             Pt = -981 Pa  ... Gauge pressure  

- Now we will use the continuity equation for points of throat area and exit.

            At*Vt = Ae*Ve

            b*ht*Vt = b*he*Ve

            Ve = ( ht / he ) * Vt

            Ve = ( 0.02 / 0.04 ) * Vt

            Ve = 0.5*Vt

           

- Now substitute the pressure at throat area ( Pt ) and the exit velocity ( Ve ) into the bernoulli's equation expressed before:

            Pt + 0.5*ρa*Vt^2 = 0 + 0.5*ρa*( 0.5*Vt )^2

            -981  = 0.5*ρa*( 0.25*Vt^2 - Vt^2 )

            -981 = - 0.1875*ρa*Vt^2

            Vt^2 = 981 / ( 0.1875*1.23 )

            Vt = √4253.65853

            Vt = 65.22 m/s

- The flow rate ( Q ) of air in the venturi is as follows:

            Q = At*Vt

            Q = ( 0.02 )*( 65.22 )

            Q = 1.3044 m^3 / s   ..... Answer part a

- We will apply the bernoulli's principle between the points of throat and point 2.

Assuming no changes in elevation between two points and the effect of friction forces on the fluid ( air ) are negligible.

                       Pt + 0.5*ρa*Vt^2 = P2 + 0.5*ρa*V2^2

- To determine the gauge pressure at point 2 ( P2 ) we can make use of the barometer principle.

Therefore from Barometer principle, we have:

              Patm - P2-abs = pw*g*ΔH2

              101,325 - P2-abs = 1000*9.81*0.05

              P2-abs = 101,325 - 490.5

              Pt-abs = 100834.5 Pa ..... Absolute pressure

- We will convert the absolute pressure into gauge pressure by the following relation:

             P2 = P2-abs - Patm

             Pt = 100,344 - 100834.5

             Pt = -490.5 Pa  ... Gauge pressure            

- Now substitute the pressure at point 2 ( P2 )  bernoulli's equation expressed before:

            Pt + 0.5*ρa*Vt^2 = P2 + 0.5*ρa*( V2 )^2

            ( Pt - P2 ) + 0.5*ρa*Vt^2 = 0.5*ρa*( V2 )^2

            2*( Pt - P2 ) / ρa + Vt^2 = V2^2

            2*( -981 + 490.5 ) / 1.23 + 65.22^2 = V2^2

            -981/1.23 + 4253.6484 = V2^2

            V2 = √3456.08742

            V2 = 58.79 m/s

- The flow rate ( Q ) of air in the venturi remains constant is as follows:

            Q = A2*V2

            Q = b*h2*V2

            h2 = Q / b*V2  

            h2 = 1.3044 / ( 0.06*58.79)

            h2 = 0.37 m      ..... Answer part b

- We will apply the bernoulli's principle between the points of inlet and exit.

Assuming no changes in elevation between two points and the effect of friction forces on the fluid ( air ) are negligible.

                       Pi + 0.5*ρa*Vi^2 = Pe + 0.5*ρa*Ve^2

- Now we will use the continuity equation for points of inlet area and exit.

            Ai*Vi = Ae*Ve

            b*hi*Vi = b*he*Ve

            Vi = ( he / hi ) * Ve

            Vi = ( 0.04 / 0.04 ) * 0.5*Vt

            Vi = Ve = 0.5*Vt = 0.5*65.22 = 32.61 m/s

- Now substitute the velocity at inlet in bernoulli's equation expressed before:

            Pi + 0.5*ρa*Vi^2 = 0 + 0.5*ρa*( Ve )^2

           

Since, Vi = Ve then:

           Pi = Pe = 0 ( gauge pressure ).

           Pi = Pe = Patm = 101.325 KPa

Comment: If the viscous effects are considered then the Pressure at the inlet must be higher than the exit pressure to do work against the viscous forces to drive the fluid through the venturi assuming the conditions at every other point remains same.

8 0
3 years ago
IV. An annealed copper strip 9 inches wide and 2.2 inches thick, is rolled to its maximum possible draft in one pass. The follow
Irina-Kira [14]

Answer:

13.9357 horse power

Explanation:

Annealed copper

Given :

Width, b = 9 inches

Thickness, $h_0=2.2$ inches

K= 90,000 Psi

μ = 0.2, R = 14 inches, N = 150 rpm

For the maximum possible draft in one pass,

$\Delta h = H_0-h_f=\mu^2R$

     $=0.2^2 \times 14 = 0.56$ inches

$h_f = 2.2 - 0.56$

     = 1.64 inches

Roll strip contact length (L) = $\sqrt{R(h_0-h_f)}$

                                             $=\sqrt{14 \times 0.56}$

                                             = 2.8 inches

Absolute value of true strain, $\epsilon_T$

$\epsilon_T=\ln \left(\frac{2.2}{1.64}\right) = 0.2937$

Average true stress, $\overline{\gamma}=\frac{K\sum_f}{1+n}= 31305.56$ Psi

Roll force, $L \times b \times \overline{\gamma} = 2.8 \times 9 \times 31305.56$

                                 = 788,900 lb

For SI units,

Power = $\frac{2 \pi FLN}{60}$  

           $=\frac{2 \pi 788900\times 2.8\times 150}{60\times 44.25\times 12}$

           = 10399.81168 W

Horse power = 13.9357

6 0
3 years ago
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