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Savatey [412]
2 years ago
15

In Florida a curb indicates and area where parking is prohibited

Engineering
2 answers:
lozanna [386]2 years ago
8 0
Curb striping or painting is used in drop-off and pick-up zones to clarify parking and other curb use rules. The color painted on curbs means: White (or no color): Parking allowed, unless restricted or limited by signs. Blue: Parking for the disabled only.
oksian1 [2.3K]2 years ago
8 0

Answer:

A curb is an Area generally not meant for parking with exceptions

Explanation:

A curb is is like a restraint placed on something as with roads in Florida, In Florida there are different colors used to differentiate the types of curbs found on the road and they are:

  • Yellow : this is used to indicate an area where parking is strictly forbidden like at road intersections or places that parking might pose a Traffic threat or environmental hazard.
  • Red : this indicates that no form of stopping, parking or standing is permitted in that area
  • blue : areas marked with blue are areas meant for disabled persons to park or their driver might park there for them
  • white : this signifies that the area is not for parking but to drop off passenger or mails
  • green : signifies parking for a limited time. parking more than the limited time might attract a fine

A curb is area that parking is generally not permitted with exceptions as seen with the different colors used to mark the curbs.

You might be interested in
A lagoon is designed to accommodate an input flow of 0.10 m^3/s of nonconservative pollutant with concentration 30 mg/L and deca
dexar [7]

Answer:

Volume of the lagoon required for the decay process must be larger than 86580 m³ = 8.658 × 10⁷ L

Explanation:

The lagoon can be modelled as a Mixed flow reactor.

From the value of the decay constant (0.2/day), one can deduce that the decay reaction of the pollutant is a first order reaction.

The performance equation of a Mixed flow reactor is given from the material and component balance thus:

(V/F₀) = (C₀ - C)/((C₀)(-r)) (From the Chemical Reaction Engineering textbook, authored by Prof. Octave Levenspiel)

V = volume of the reactor (The lagoon) = ?

C₀ = Initial concentration of the reactant (the pollutant concentration) = 30 mg/L = 0.03 mg/m³

F₀ = Initial flow rate of reactant in mg/s = 0.10 m³/s × C₀ = 0.1 m³/s × 0.03 mg/m³ = 0.003 mg/s

C = concentration of reactant at any time; effluent concentration < 10mg/L, this means the maximum concentration of pollutant allowed in the effluent is 10 mg/L

For the sake of easy calculation, C = the maximum value = 10 mg/L = 0.01 mg/m³

(-r) = kC (Since we know this decay process is a first order reaction)

This makes the performance equation to be:

(kVC₀/F₀) = (C₀ - C)/C

V = F₀(C₀ - C)/(kC₀C)

k = 0.2/day = 0.2/(24 × 3600s) = 2.31 × 10⁻⁶/s

V = 0.003(0.03 - 0.01)/(2.31 × 10⁻⁶ × 0.03 × 0.01)

V = 86580 m³

Since this calculation is made for the maximum concentration of 10mg/L of pollutant in the effluent, the volume obtained is the minimum volume of reactor (lagoon) to ensure a maximum volume of 10 mg/L of pollutant is contained in the effluent.

The lower the concentration required for the pollutant in the effluent, the larger the volume of reactor (lagoon) required for this decay reaction. (Provided all the other parameters stay the same)

Hope this helps!

5 0
2 years ago
A utility generates electricity with a 36% efficient coal-fired power plant emitting the legal limit of 0.6 lb of SO2 per millio
Mama L [17]

Answer:

a) 570 kWh of electricity will be saved

b) the amount of  SO₂ not be emitted or heat of electricity saved is 0.00162 ton/CLF

c) $1.296 can be earned by selling the SO₂ saved by a single CFL

Explanation:

Given the data in the question;

a) How many kilowatt-hours of electricity would be saved?

first, we determine the total power consumption by the incandescent lamp

P_{incandescent} = 75 w × 10,000-hr = 750000 wh = 750 kWh

next, we also find  the total power consumption by the fluorescent lamp

P_{fluorescent} = 18 × 10000 = 180000 = 180 kWh

So the value of power saved will be;

P_{saved} = P_{incandescent}  - P_{fluorescent}

P_{saved} = 750 - 180

P_{saved}  = 570 kWh

Therefore, 570 kWh of electricity will be saved.

now lets find the heat of electricity saved in Bituminous

heat saved = energy saved per CLF / efficiency of plant

given that; the utility has 36% efficiency

we substitute

heat saved =  570 kWh/CLF / 36%

we know that; 1 kilowatt (kWh) = 3,412 btu per hour (btu/h)

so

heat saved =  570 kWh/CLF / 0.36 × (3412 Btu / kW-hr (

heat saved = 5.4 × 10⁶ Btu/CLF

i.e eat of electricity saved per CLF is 5.4 × 10⁶

b) How many 2,000-lb tons of SO₂ would not be emitted

2000 lb/tons = 5.4 × 10⁶ Btu/CLF

0.6 lb SO₂ / million Btu = x

so

x = [( 5.4 × 10⁶ Btu/CLF ) × ( 0.6 lb SO₂ /  million Btu )] / 2000 lb/tons

x = [( 5.4 × 10⁶ Btu/CLF ) × ( 0.6 lb SO₂ )] / [ ( 10⁶) × ( 2000 lb/ton) ]

x = 3.24 × 10⁶ / 2 × 10⁹

x = 0.00162 ton/CLF

Therefore, the amount of  SO₂ not be emitted or heat of electricity saved is 0.00162 ton/CLF

c)  If the utility can sell its rights to emit SO2 at $800 per ton, how much money could the utility earn by selling the SO2 saved by a single CFL?

Amount = ( SO₂ saved per CLF ) × ( rate per CFL )

we substitute

Amount = 0.00162 ton/CLF × $800

= $1.296

Therefore; $1.296 can be earned by selling the SO₂ saved by a single CFL.

3 0
3 years ago
What are the minimum and maximum required footing projections for a concrete footing having a thickness of 8 inches
SpyIntel [72]

The minimum and maximum required footing projections for a concrete footing having a thickness of 8 inches will be 4 inches and 8 inches.

<h3>What is projection?</h3>

It should be noted that footing projections are important for construction purposes

In this case, the minimum and maximum required footing projections for a concrete footing having a thickness of 8 inches will be 4 inches and 8 inches.

Learn more about projection on:

brainly.com/question/3703881

#SPJ12

8 0
1 year ago
Check Your Understanding: True Stress and Stress A cylindrical specimen of a metal alloy 47.7 mm long and 9.72 mm in diameter is
VARVARA [1.3K]

Answer:

The answer is "583.042533 MPa".

Explanation:

Solve the following for the real state strain 1:

\varepsilon_{T}=\In \frac{I_{il}}{I_{01}}

Solve the following for the real stress and pressure for the stable.\sigma_{r1}=K(\varepsilon_{r1})^{n}

K=\frac{\sigma_{r1}}{[\In \frac{I_{il}}{I_{01}}]^n}

Solve the following for the true state stress and stress2.

\sigma_{r2}=K(\varepsilon_{r2})^n

     =\frac{\sigma_{r1}}{[\In \frac{I_{il}}{I_{01}}]^n} \times [\In \frac{I_{i2}}{I_{02}}]^n\\\\=\frac{399 \ MPa}{[In \frac{54.4}{47.7}]^{0.2}} \times [In \frac{57.8}{47.7}]^{0.2}\\\\ =\frac{399 \ MPa}{[ In (1.14046122)]^{0.2}} \times [In (1.21174004)]^{0.2}\\\\ =\frac{399 \ MPa}{[ In (1.02663509)]} \times [In 1.03915873]\\\\=\frac{399 \ MPa}{0.0114161042} \times 0.0166818905\\\\= 399 \ MPa \times 1.46125948\\\\=583.042533\ \ MPa

4 0
3 years ago
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
2 years ago
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