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SpyIntel [72]
3 years ago
6

Type the correct answer in the box. Spell all words correctly.

Engineering
2 answers:
sesenic [268]3 years ago
6 0

Answer:

Chemical Engineers use chemistry, math and physics to design and use to make chemical products. The fibers in clothing are designed by chemical engineers.

Arlecino [84]3 years ago
6 0

Answer:

Textile engineering

You might be interested in
Steam enters a heavily insulated throttling valve at 11 MPa, 600°C and exits at 5.5 MPa. Determine the final temperature of the
7nadin3 [17]

Answer: the final temperature of the steam 581.5 °C

Explanation:

Given that;

P₁ = 11 MPa

T₁ = 600°C

exit at; P₂= 5.5 MPa

Now from superheated steam table( p=11 MPa, T=600°C)

h₁ = 3615 kJ/kg  

h₁ = h₂ ( by throttling process and adiabatic isentholpic )

from saturated steam table at; ( h= 3615 kJ/kg, P= 5.5 MPa )

Temperature = 581.5 °C

Therefore the final temperature of the steam 581.5 °C

8 0
3 years ago
What are the specifications state that all work shall be done?
Elodia [21]

Answer:

The description including its scope is presented throughout the section below.

Explanation:

  • Such operation must be carried out in compliance with all statutes, legislation, building standards, guidelines, and rules relating to that same task, not all of which are restricted to either the U.S Disability Act, the Ecological laws as well as the workplace Safety Act as modified.
  • This same consultant shall appoint and could be completely liable for almost all processes and sequences just for conducting the Job.
4 0
3 years ago
The number of vacancies in some hypothetical metal increases by a factor of 3 when the temperature is increased from 1020 ˚C to
weeeeeb [17]

Answer:

first step here is to substitute the 3 of your two equations into the second;

3 Ne^(-Q_v/k(1293)) = Ne^(-Q_v/k(1566))

Since 'N' is a constant, we can remove it from both sides.

We also want to combine our two Q_v values, so we can solve for Q_v, so we should put them both on the same side:

3 = e^(-Q_v/k(1293)) / e^(-Q_v/k(1566))

3 = e^(-Q_v/k(1293) + Q_v/k(1566) ) (index laws)

ln (3) = -Q_v/k(1293) + Q_v/k(1566) (log laws)

ln (3) = -0.13Q_v / k(1566) (addition of fractions)

Q_v = ln (3)* k * 1566 / -0.13 (rearranging the equation)

Now, as long as you know Boltzmann's constant it's just a matter of substituting it for k and plugging everything into a calculator.

6 0
4 years ago
The assembly consists of a brass shell (1) fully bonded to a ceramic core (2). The brass shell [E = 93 GPa, α= 15.1 × 10−6/°C] h
marshall27 [118]

Answer:

ΔT = 62.11°C

Explanation:

Given:

- Brass Shell:

       Inner Diameter d_i = 32 mm

       Outer Diameter d_o = 39 mm

       E_b = 93 GPa

       α_b = 15.1*10^-6 / °C

- Ceramic Core:

       Outer Diameter d_o = 32 mm

       E_c = 310 GPa

       α_c = 3.2*10^-6 / °C

- Unstressed @ T = 8°C

- Total Length of the cylinder L = 160 mm

Find:

Determine the largest temperature increase Δ⁢t that is acceptable for the assembly if the normal stress in the longitudinal direction of the brass shell must not exceed 60 MPa.

Solution:

- Since, α_b > α_c the brass shell is in compression and ceramic core is in tension. The stress in shell is given as б_a:

                              б_b = - 60 MPa

- The force equilibrium can be written as:

                          б_b*A_b + б_c*A_c = 0

Where, б_b is the stress in core

            A_b is the cross sectional area of the shell

            A_c is the cross sectional area of the core

                           б_b*pi*( d_o^2 - d_i^2) / 4  + б_c*pi*( d_i^2) / 4 = 0

                           б_b*( d_o^2 - d_i^2)  + б_c*( d_i^2) = 0

                           б_c = - б_b*( d_o^2 - d_i^2) / ( d_i^2)

Plug in the values:

                           б_c = 60*( 0.039^2 - 0.032^2) / ( 0.032^2)

                           б_c =  29.121 MPa , б_b = - 60 MPa

-  The total strains in both brass shell and ceramic core is given by:

                           ξ_b = α_b*ΔT + б_b / E_b

                           ξ_c = α_c*ΔT + б_c / E_c

- The compatibility relation is:

                           ξ_b = ξ_c

                           α_b*ΔT + б_b / E_b = α_c*ΔT + б_c / E_c

                           ΔT*(α_b - α_c ) = б_c / E_c - б_b / E_b

                           ΔT = [ б_c / E_c - б_b / E_b ] / (α_b - α_c )

Plug in values and solve:

                           ΔT = [ 0.029121 / 310 + 0.06 / 93 ]*10^6 / (15.1 - 3.2 )

                           ΔT = 62.11°C

8 0
3 years ago
Cooling water for a chemical plant must be pumped from a river 2500 ft from the plant site. Preliminary design cans for a flow o
Vesna [10]

Answer:

The power cost savings for the 8 inches pipe offsets the increased cost for the pipe therefore to save costs the 8-inch pipe should be used

Explanation:

The given parameters in the question are;

The distance of the river from the the site, d = 2,500 ft.

The planned flow rate = 600 gal/min

The diameter of the pipe, d = 6-in.

The pipe material = Steel

The cost of pumping = 3 cents per kilowatt-hour

The Bernoulli's equation is presented as follows;

\dfrac{P_a}{\rho} + g\cdot Z_a + \dfrac{V^2_a}{2} + \eta\cdot W_p = \dfrac{P_b}{\rho} + g\cdot Z_b + \dfrac{V^2_b}{2} +h_f +W_m

{P_a} = {P_b} = Atmospheric \ pressure

Z_a  =  Z_b

Vₐ - 0 m/s (The river is taken as an infinite source)

W_m = 0

The head loss in 6 inches steel pipe of at flow rate of 600 gal/min = 1.19 psi/100 ft

Therefore; h_f = 1.19 × 2500/100 = 29.75 psi

\eta\cdot W_p = \dfrac{V^2_b}{2} +h_f

V_b = Q/A_b = 600 gal/min/(π·(6 in.)²/4) = 6.80829479 ft./s

V_b ≈ 6.81 ft./s

The pressure of the pump = P =  62.4 lb/ft³× (6.81 ft./s)²/2 + 29.75 psi ≈ 30.06 psi

The power of the pump = Q·P ≈ 30.06 psi × 600 gal/min = 7,845.50835 W

The power consumed per hour = 7,845.50835  × 60  × 60 W

The cost = 28,243.8301 kW × 3  = $847.31  per hour

Annual cost =  $847.31 × 8766 = $7,427,519.46

Pipe  cost = $15/ft × 2,500 ft = $37,500

Annual charges = 20% × Installed cost = 0.2 × $37,500 = $7,500

Total cost = $37,500 + $7,500 + $7,427,519.46 = $7,475,519.46

For the 8-in pipe, we have;

V_b = Q/A_b = 600 gal/min/(π·(8 in.)²/4) = 3.83 ft./s

h_f = 1.17 ft/100 feet

Total head loss = (2,500 ft/100 ft) × 1.17 ft. = 29.25 ft.

h_p = \dfrac{V^2_b}{2 \cdot g} +h_f

∴ h_p = (3.83 ft./s)²/(2 × 32.1740 ft/s²) + 29.25 ft. ≈ 29.5 ft.

The power of the pump = ρ·g·h × Q

Power of pump = 62.4 lb/ft³ × 32.1740 ft/s² × 29.5 ft.× 600 gal/min = 3,363.8047 W

The cost power consumed per annum = 3,363.8047 W × 60 × 60 × 3 × 8766 = $3,184,608.1

The Cost of the pipe = $20/ft × 2,500 ft. = $50,000

The total cost plus charges = $3,184,608.1 + $50,000 + $10,000 = $3,244,608.1

Therefore it is more affordable to use the 8-in pipe which provides substantial savings in power costs

8 0
3 years ago
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